[go: up one dir, main page]

EP0061412A1 - Method and apparatus for the manufacture of synthetic-foam sheets - Google Patents

Method and apparatus for the manufacture of synthetic-foam sheets Download PDF

Info

Publication number
EP0061412A1
EP0061412A1 EP82430006A EP82430006A EP0061412A1 EP 0061412 A1 EP0061412 A1 EP 0061412A1 EP 82430006 A EP82430006 A EP 82430006A EP 82430006 A EP82430006 A EP 82430006A EP 0061412 A1 EP0061412 A1 EP 0061412A1
Authority
EP
European Patent Office
Prior art keywords
container
conveyor
mixture
cylinder
foam
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Granted
Application number
EP82430006A
Other languages
German (de)
French (fr)
Other versions
EP0061412B1 (en
Inventor
Jean Poncet
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Sunkist Chemical Machinery Ltd Te Taipei Taiwan
Original Assignee
Individual
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Individual filed Critical Individual
Priority to AT82430006T priority Critical patent/ATE14397T1/en
Publication of EP0061412A1 publication Critical patent/EP0061412A1/en
Application granted granted Critical
Publication of EP0061412B1 publication Critical patent/EP0061412B1/en
Expired legal-status Critical Current

Links

Images

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C44/00Shaping by internal pressure generated in the material, e.g. swelling or foaming ; Producing porous or cellular expanded plastics articles
    • B29C44/20Shaping by internal pressure generated in the material, e.g. swelling or foaming ; Producing porous or cellular expanded plastics articles for articles of indefinite length
    • B29C44/32Incorporating or moulding on preformed parts, e.g. linings, inserts or reinforcements
    • B29C44/322Incorporating or moulding on preformed parts, e.g. linings, inserts or reinforcements the preformed parts being elongated inserts, e.g. cables
    • B29C44/324Incorporating or moulding on preformed parts, e.g. linings, inserts or reinforcements the preformed parts being elongated inserts, e.g. cables the preformed parts being tubular or folded to a tubular shape
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C44/00Shaping by internal pressure generated in the material, e.g. swelling or foaming ; Producing porous or cellular expanded plastics articles
    • B29C44/34Auxiliary operations
    • B29C44/36Feeding the material to be shaped
    • B29C44/46Feeding the material to be shaped into an open space or onto moving surfaces, i.e. to make articles of indefinite length
    • B29C44/461Feeding the material to be shaped into an open space or onto moving surfaces, i.e. to make articles of indefinite length dispensing apparatus, e.g. dispensing foaming resin over the whole width of the moving surface
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10TECHNICAL SUBJECTS COVERED BY FORMER USPC
    • Y10STECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10S264/00Plastic and nonmetallic article shaping or treating: processes
    • Y10S264/84Conversion of foamed resinous buns into foamed billets having geo metrical crosssections

Definitions

  • the present invention relates to a method and a device for manufacturing strips of polymer foam and product obtained.
  • the technical sector of the invention is that of equipment for the implementation of flexible or rigid foam strips.
  • the currently known continuous casting methods consist, for the most part, in distributing the liquid reactive mixture as uniformly as possible over the width of an inclined conveyor, formed by a bottom and by two side walls which move perpendicular to the liquid distribution.
  • This distribution of a mixture of liquid reactants, which is not very viscous, and of rapid reactivity, implies a retention zone capable of containing the liquid spilled for the time necessary and sufficient for this operation.
  • the inclination of the conveyor is generally 4 to 6 ° over the length necessary for the expansion of the foam and its gelation: between fifteen and twenty meters. The movement is then made on a horizontal plane to the cross cutting equipment: about fifty meters from the casting point.
  • the most conventional devices include a casting head animated with a transverse movement back and forth and the reactant retention zone is formed, upstream by the bottom of the conveyor, generally consisting of a sheet of flexible material: sheet of paper or of polyethylene, laterally by continuously scrolling walls made of the same material as that of the bottom and downstream, by the product itself which enters its initial reactive phase called "cream line".
  • cream line designates the state of the mixture of reactants occurring immediately after the liquid phase - and in which this mixture reaches a high viscosity. preceding the formation of the foam.
  • the viscous product adheres to the bottom support and constitutes, constantly renewed, a barrier to the flow of the liquid mixture along the slope of the conveyor.
  • an obstacle is placed downstream of the casting head at the start of manufacture, the role of which is to retain the liquid mixture at start-up.
  • the upstream wall is always formed by the bottom of the conveyor which must necessarily be inclined.
  • the main drawback, arising from this design, is the difficulty of controlling the parasitic flow of the liquid phase of the reactants, below the line, of cream.
  • the mixture As has just been exposed, the mixture, during its expansion, progressively passes from the liquid state to the solid state, the finished product being able to be rigid or flexible depending on the degree of crosslinking of the polymer.
  • the rapidly viscous then pasty state of the mixture causes against the walls of the shaper whatever it is: a closed or open mold on top, a retainer which slows down the expansion of the cells coming into contact with the walls.
  • a known method and device consists in lining the lateral movable walls with a polyethylene film drawn first at a determined angle to the point of completion of the expansion of the foam, from which, after forming a fold , it then accompanies the foam block until it leaves the conveyor.
  • the foam in formation is compressed using weighted pads bearing on the upper face of the block, by means of a strip of paper or a strip of non-woven fiber, which accompanies the block when moving on the conveyor.
  • the drawbacks of the first method lie in the fact that it requires the use of sheets of a very flexible material with a view to its deformability.
  • a material preferably polyethylene, is relatively fragile and currently expensive since it is a petroleum derivative.
  • the fold formed at the end point of the expansion of the foam leaves traces on the lateral faces of the strips, which make it necessary to straighten the flanks, which results in significant material piercing.
  • the drawback of the third method lies in the complexity of the device for varying the width of the strip of foam during manufacture.
  • the rigid foam sheets of controlled thickness and each side of which is made up of a protective material: paper, fabric, plasterboard, wood, etc. are generally manufactured continuously, in standard width preferably one meter. twenty centimeters, by means of horizontal conveyors known as double belts, one lower of which supports a band which receives the reactive mixture and the other upper comprises a band which limits the expansion of the product and ensures, in addition to sizing, the flatness of the upper side.
  • Another objective of the invention is to produce strips of flexible polymer foam with a rectangular cross section whose upper face is flat.
  • Another objective of the invention is the manufacture of rigid foam plates loaded and / or lightened, in particular plates having in their thickness longitudinal and parallel channels between them while the currently known techniques only allow the production of solid panels in virgin matter.
  • the volume of the container is in particular determined by operating over at least its length, so that the retention zone defines the width of the foam strip.
  • the device according to the invention for producing strips of polymer foam obtained from a mixture of liquid reactants generating an expanded foam and comprising a container, means for continuously introducing into this container , said mixture of liquid reactants and a U-shaped conveyor, animated by a continuous movement on which the foam is deposited to take the form of a strip of a rectangular cross section, characterized in that the container has a front wall, a rear wall and two side walls, the front and rear walls of which also constitute the bottom of the container and in that the front wall, which is situated on the side of the conveyor, is a curved wall constituted by a cylinder, driven in rotation around a axis substantially horizontal in the same direction and at the same speed as the conveyor and in that the edges of the side walls, located on the side of the curved wall, are of a circular outline and partially surround the cylinder in order to allow the relative movement of the cylinder and of the other walls while ensuring the sealing of the container.
  • the upper edge of the rear wall and the side walls of the container are located at a level higher than that of the front wall, which tangents a substantially horizontal surface over which the mixture of reactants in liquid phase flows, which horizontal surface is animated. of a continuous movement under the effect of the conveyor.
  • rear wall, side walls includes means for obtaining its pivoting around the axis of said cylinder in order to raise or lower said assembly relative to said horizontal surface in order to modify the volume of the container. ; and to immobilize in position said assembly after adjustment.
  • the rear wall of the container is a curved wall formed by a cylinder, driven in rotation in the same direction as the front cylinder, which cylinders are mounted on two axes parallel to each other and are substantially tangent, the line of tangency constituting the bottom of the container and in that the side walls are parallel to each other and are above the cylinders and their lower edge is delimited by two concurrent circular lines at a point located in the vicinity of said line of tangency, which side walls partially surround the cylinders in order to allow on the one hand the rotation of the cylinders and on the other hand the relative movement of the rear cylinder / side walls assembly around the front cylinder while ensuring the tightness of the container.
  • the rear cylinder has a larger diameter than the front cylinder and is rotated at a slower speed than that of said front cylinder.
  • the rear cylinder is immersed in a solvent tank and is subjected to the action of a squeegee extending in the longitudinal direction of the cylinder to detach the polymerized particles adhering thereto at its periphery.
  • Each of the side walls has a counter plate extending from the side of said horizontal surface on which the mixture of reactants in the liquid phase is deposited to seal at the junction of the side walls and said surface, which counter plates are adjustable in position on the walls.
  • Said side walls include means for bringing them towards one another or away from one another and for immobilizing them in position.
  • At least one of said cylinders comprises a bundle of conduits which are parallel to each other and to the axis of rotation of the cylinder, in which conduits a coolant is circulated in order to raise or lower the temperature of the cylinder and correspondingly the temperature of the mixture of reactants in liquid phase.
  • the curved wall formed by said cylinder located at the front of the container on the side of the conveyor and the rear wall of the container, define a space in which a flexible sheet has passed, which partially wraps around said cylinder on which it moves. in the container, which sheet continues to run while being supported by the conveyor and constitutes said horizontal surface on which the mixture of reactants is deposited.
  • the flexible sheet is applied against the lower part of said front cylinder, below. from the bottom of the container, by means of a roller subjected to the action of elastic means.
  • the flexible sheet is applied against the lower part of the rear cylinder, below the line of tangency of the two cylinders by means of a roller subjected to the action of elastic means, which sheet is then passed between the two cylinders and partially surrounds the front cylinder from above to extend tangentially thereto in a substantially horizontal position.
  • the mixture of which is introduced at the source into the container a characteristic is that it comprises at least one tube passing through each of the walls.
  • lateral, which tubing is slidably mounted to be positioned in the casting head and has along its length openings to ensure the distribution of the mixture in the liquid state in said head.
  • the tubing consists of several coaxial tubes, arranged in the extension of one another and of tapering section with respect to the circulation of the mixture, so as to reserve between them substantially annular spaces of the same section, which corresponds approximately to the section of the smallest central tube.
  • the device according to the invention also comprises a substantially horizontal plate, of a width at least equal to that of the conveyor and the upper face of which is tangent to the front cylinder of the container, which tray extends from said front cylinder to. 'to the conveyor and supports the sheet on which the foam develops.
  • the U-shaped conveyor consists of a mat carrying the flexible sheet on which the foam develops and whose side walls are constituted by two flexible sheets, each from a vertical roller located at the front of the device on the container side, which sheets extend over the length of the conveyor and are wound around a vertical roller situated at the rear of the device, said sheets moving at the speed of the mat while being attached to the side of their lower edge along the lateral edges of said sheet, carried by the conveyor, a characteristic consists in the fact that it furthermore comprises parallel and close to each of the internal faces from the side walls of the conveyor, another inclined flexible sheet, which comes from a roll located on the side of said container, extends over at least the part of the device where the reactants deposited in liquid phase on said horizontal sheet enter into reaction and develop until the total expansion of the foam, which sheet moves in this part in a rectilinear direction from the inlet to the outlet of the device and from the bottom up to be supported by a roller located above of the conveyor, its inclination being such that its lateral edges
  • the inclined parts of said sheet are located above the conveyor and the casting head and one of the parts is inclined up and down and folded along a parallel rectilinear member and adjoining the horizontal sheet and the other part is returned from bottom to top at the same inclination as that of said first part.
  • the device according to the invention comprising a lower conveyor, carrying a flexible sheet on which the mixture of reactants is deposited and a second conveyor disposed above said conveyor lower and parallel to it and on which. is applied a flexible sheet on the lower strand of the upper mat, which conveyors define a space which determines the thickness of the rigid foam panels, is characterized in that the container in which the liquid reactants are introduced is movable in the longitudinal direction of the device and comprises means for being immobilized in position relative to the conveyors,
  • the plate which extends between the container and the lower conveyor, consists of at least two thin plates, mutually parallel and adjacent, which plates are telescopic to adjust the length of the plate so de-connect the container and the conveyor.
  • This device comprises, in the space existing between the lower conveyor and the upper conveyor, bars parallel to each other and arranged in the same plane, which bars are cantilevered and are fixed to the structure of the device on the side of said container and extend towards the conveyors, so that their free end, which is located between said conveyors, is located substantially at the place where the solidification of the foam occurs.
  • Each of these bars is surrounded by a sheath slightly larger than the bar so that it can be moved along the latter under the effect of the foam during its expansion in order to continuously produce and delimit channels in the foam panels.
  • the invention also relates to a new product consisting of a rigid foam panel whose large faces are covered with sheets of protective material, characterized in that it comprises, in its thickness, parallel channels between them, the peripheral wall is protected by a sheath adhering to the foam.
  • the upstream wall of the retention zone formed either by the rear cylinder or by the wall of the tank, is always at an altitude higher than that of the front cylinder.
  • the downstream wall is formed, at its lower part, by the flexible bottom support conforming to the shape of the front cylinder and at its upper part by the line of cream with this peculiarity that the retained volume of reactive liquid, therefore of the water table.
  • the flow which determines the height of the block can be controlled to a large extent, approximately in a proportion of 1 to 2.
  • the substantially horizontal position of the conveyor no longer causes parasitic flow of the liquid phase under the expanding phase, a drawback already mentioned on inclined conveyors and which requires a minimum speed.
  • the speed can be reduced as much as the reactivity of the mixture allows, resulting in a proportional reduction in the length of the installations.
  • the invention offers the possibility of regulating the temperature of the cylinders or the tank. It being recalled that the foaming reaction generates heat, it is important to be able to maintain the mixture and the equipment at a constant temperature. It is preferable to use a heat transfer fluid passing through the cylinders and capable of removing the calories produced or, on the contrary, providing them if necessary.
  • the arrival of the reactive liquid can be carried out either by runoff on a chute, or at the source by two lateral pipes crossing the movable sides and each constituted by a series of nozzles: concentric with decreasing sections from upstream to downstream, so that the nozzles have all the same section or neighboring sections to avoid any turbulence in the liquid mixture and to ensure the distribution of the mixture in the container.
  • the apparatus as described above can easily be adapted to existing conveyors, in particular for the manufacture of flexible foam, without losing the advantage of the formation of the cream line on a horizontal plane.
  • This adaptation can be extended to rigid foam production machines, known as "double band” machines, while retaining the option generally offered by these machines, of adjusting the distance between the casting head, here the retention zone, and the inlet. of the double belt conveyor.
  • the method and the device according to the invention finally allow the manufacture of rigid foam sheets.
  • the adoption of a source-supplied cylinder head allows placing a device capable of creating longitudinal channels in the thickness of the panel being formed and thus achieving a significant saving of raw material.
  • FIGS. 1 to 7 of the drawing illustrate the invention in an embodiment for obtaining strips of flexible polymer foam.
  • the device of Figure 1 consists of a conveyor 1, extending in a substantially horizontal plap whose supporting strand supports a flexible sheet 2, from a roll 3.
  • This sheet 2, for example of paper is of 'first passed through a casting head 4 and is supported, while being able to slide, on an intermediate plate 5, arranged between the head 4 and the conveyor 1.
  • the plate 5 and the carrying strand 1a of the conveyor 1 are substantially in the same plane.
  • the side walls of the conveyor 1 are formed in a known manner by flexible sheets 6, from two rollers 7.
  • the rollers 7 are arranged perpendicular to the conveyor 1 and the sheets 6 are adjacent to the side edges of the horizontal sheet 2.
  • the rollers 7 are for example located at level of the drum before lb of the conveyor 1. We will return later to this figure to complete its description concerning other arrangements relating to the invention.
  • the casting head 4 is shown in Figures 3 to 7 of the drawing.
  • pouring head The device in which the liquid phase reactants are introduced with a view to mixing them and ensuring the function of distributor of this liquid mixture is called pouring head before its expansion occurs until the final phase where it takes the consistency of 'a foam.
  • the method consists in determining the volume of a container to form a retention zone for the mixture of reactants in the liquid phase and the level of this mixture is maintained at a level slightly higher than the plane in which the sheet 2 moves. , so that the primary phase of the expansion of the mixture and its expansion takes place outside the container, on said sheet 2, which is moved in the direction of arrow F to bring the mixture in reaction into contact with the walls of the conveyor 1/2/6 which give the foam strip its final shape, this being for example of a rectangular cross section.
  • Figures 3 to 7 show a preferred embodiment of the casting head, which consists of a container 8 composed of two cylinders of the same length 9/10 and two side walls 11.
  • the cylinders 9/10 are of different diameters, so that the cylinder 9 is smaller than the cylinder 10.
  • These cylinders are parallel to each other and are arranged horizontally and transversely to the conveyor 1.
  • the cylinder 9 is located near the plate 5 and is very close from the other cylinder 10 so as to leave a slight space between them for the passage of a film, for example a sheet of paper 2. In this position, the cylinders are substantially tangent and the line of tangency marked 12 constitutes the lower end part of the container.
  • This comprises two animated curved front / rear walls, which are constituted by said cylinders 9/10 as well as side walls 11 which are arranged above the cylinders, are parallel to each other and extend perpendicular to the generatrices of said cylinders 9 / 10. Their lower edge is formed by two curved lines lla / llb which converge at point llc, which is located in the vicinity of the line of tangency marked 12.
  • Line lla is a circular line of a ryon R 1 having as its center the axis of rotation of the cylinder 10.
  • This circular line 11a closely circumvents the periphery of the cylinder 10.
  • the line llb is a circular line of. radius R 2 , having as its center the axis of rotation of the cylinder 9.
  • the circular line 11b bypasses the periphery of the cylinder 9 and is supported on the sheet of paper 2.
  • the curved line 11b is extended by a straight line 11d s' extending above the plate 5.
  • the upper part of the cylinder 9 is substantially tangent to the plane in which the plate 5 is located and in which the flexible sheet 2 moves.
  • the sheet 2 is first supported on a first roller 3a; mounted to rotate freely on the machine structure and is applied against the cylinder 10 by a roller 3b.
  • the set of cylinders 9/10 and side walls 11 is pivotally mounted around the axis of the cylinder 9, so that the volume of the mixture retention zone 8 can vary depending on the angular position of said set.
  • the angular movement a is for example 15 °.
  • the cylinder 10 being in its lower extreme position, the volume of the retention zone 8 is maximum.
  • the cylinder 10 is in its extreme upper position and the volume of said zone 8 is minimum.
  • each wall 11 comprises, on the side of the plate 5, a counter plate 13 intended to mask the vacuum existing between the line 11d and the sheet 2
  • This counter plate 13 has, at its lower part, a circular edge 13a extended by a straight line 13b.
  • the lower edge of the plate 13 thus follows the contour of the upper part of the cylinder 9 and extends over part of the plate 5.
  • the counter plates 13 also have a curved opening 13c to allow their positioning on the side walls 11 and their fixing is ensured for example by means of two bolts 14 or by any other equivalent means.
  • the cylinders 9/10 are rotated in the direction of the arrows F2 which is also the direction of the conveyor. 1.
  • the cylinder 9 is driven at the speed of the conveyor 1.
  • the cylinder 10 rotates at a slower speed.
  • the admission of the liquid mixture into the container 8 can be carried out in two ways either by means of a dispensing head 15 which pours the liquid mixture onto a distribution chute 16, situated above the cylinder 10, or by means of two horizontal tubes 17 introducing the source liquid through the side walls of the container. Each of these tubes passes through one of the side walls 11 and brings the mixture of reactants without turbulence into the container.
  • tubing 17 is illustrated in Figures 14/15 of the drawing. It consists of several coaxial tubes 17a / 17b / 17c / 17d placed in the extension of each other so that the end of the tube 17e can reach the central area of the casting head whatever the position of the side walls 11 relative to the median axis of the head.
  • This tubing is therefore mounted adjustable in the wall 11 which it passes through and the seal, at the right of passage therein, is obtained for example by means of a lip seal 17f allowing its sliding.
  • Each of the tubes 17b / 17c / 17d reserves in combination with the one in which it is engaged and which it extends 17a / 177b / 17c, an annular space 17g / 17h / 17k substantially of the same section, which approximately corresponds to the section of the most small tube 17d.
  • the positioning of the tubes between them is obtained by means of spacers 17l, distributed around the tubes.
  • the mixed in the liquid state is thus distributed in the casting head at the same flow rate and without turbulence by the annular spaces 17g / 17h / 17k as well as by the central tube 17d.
  • the cylinders 9/10 are rotated by being mounted on two arms 18 parallel to each other and arranged on either side of the cylinders.
  • the large cylinder 10 is mounted adjustable on the supports 18 in bearings 19 mounted on slides and comprising adjustment means 19a and stop 19b to allow it to move away from or closer to the cylinder 9, and to immobilize it in position .
  • the cylinder 9 is mounted in a fixed position at one end of the arms 18.
  • the assembly is carried by bearings 20 fixed to the chassis of the machine.
  • the arms 18 and all of the elements which they carry can pivot around the axis of the cylinder 9, marked 21.
  • the roller 3b intended to press the sheet of paper against the cylinder 10, is carried by two rods 22, articulated by their middle around an axis 23 carried by a lug extending to the lower part of the arms.
  • the links 22 are subjected to the tension of a spring 24, hooked to the arms 18, so that the roller 3b is pivoted on the side of the cylinder 10.
  • the arms 18 are interconnected by a crosspiece 25 and have two extensions 26 extending perpendicularly from bottom to top. These two extensions 26 are mutually parallel and carry at their upper part a threaded rod 27, the thread of which is reversed right / left from its middle. This rod 27 is connected by one of its ends to means for driving it in rotation.
  • the angular movement of the assembly is obtained by means of one or more double-acting cylinders 32, preferably hydraulic, articulated on the one hand at 33 at the end of the mobile structure 18/25/26 and secondly at 34 on a yoke 35 fixed to the chassis of the apparatus.
  • the choice of the volume of the retention zone 8 is obtained by modifying the angle a of the line XX 1 on which the cylinders 9/10 are and / or by modifying the length of the container by displacement of the side walls 11, by acting on the screw 27.
  • the walls 11, guided in translation by the supports 30, can be brought towards one another or distant from each other symmetrically to the longitudinal axis of the device.
  • the arm 30 is held parallel to the arm 18 by means of a sliding stop 36 indented at 36a which is integral with it and which cooperates with a slide 37 extending transversely to the casting head and which is parallel to the screw 27.
  • This stop 36 extends perpendicularly to arm 30 and below it each arm 30 has a stop.
  • the adjustment of the spacing of the side walls 11 determines the width of the strip of foam obtained.
  • the liquid reactant mixture contained in the retention zone 8 and the upper level of which is substantially in the plane of the plate 5 or slightly above, is entrained in the liquid state by the flexible sheet 2, so that the expansion and expansion of the foam occur outside the container on the tray 5, the total expansion continuing on the conveyor 1.
  • the cylinder 10 which constitutes the rear pardi of the container, is partially immersed in a solvent tank 38, disposed at the lower part of the casting head.
  • This tank 38 includes a squeegee 39 extending transversely to the cylinder and held in position at a suitable angle to detach from the wall of the cylinder the particles of polymerized material which could have adhered to it.
  • the tank 38 moves with the assembly when the volume of the retention zone 8 is adjusted and its shape is such that no spillage of solvent can occur.
  • the cylinders 9/10 also comprise conduits 9a / 10a equidistant from the axis of rotation of the cylinders and extending longitudinally, parallel, to said axis of rotation.
  • the cylinders have rotating joints at their ends to seal at these locations.
  • the purpose of these conduits 9a / 10a is to channel a heat-transfer fluid, for example water, for the purpose of heating or cool the cylinders and correspondingly the mixture of reactants.
  • This design is advantageous because, since the foaming reaction generates heat, it is important to maintain the mixture and the equipment at a constant temperature. It allows in particular to control the temperature at various points in the container. For example, the rear cylinder 10 can be cooled while the cylinder 9 can be heated.
  • This consists of a cylinder 40 rotated in the direction of movement of the conveyor belt of the conveyor 1 and on which cylinder 40 is applied a sheet of paper 2 from a reel 3.
  • the partial winding of the sheet 2 on the cylinder 40 is obtained by means of a roller 41 extending parallel to said cylinder.
  • the flexible sheet 2 is supported by a horizontal plate 5 and is supported by a conveyor also horizontal.
  • the cylinder 40 covered with the flexible sheet 2, constitutes the front wall of the container into which the mixture of liquid reactants is introduced.
  • the rear and bottom walls of the container and the side walls form an assembly which can pivot around the cylinder 40 while remaining tightly applied by the side walls to the flexible sheet 2.
  • its upper part is always at a level higher than the plane of the plate 5 in which the sheet 2 moves.
  • the container consists of a rear wall 42; which partially follows the contour of the cylinder 40 and has at its lower part a "return" 42a, directed towards the side of said cylinder.
  • a space 43 is reserved between the parts 42a and the cylinder, to allow the passage of the flexible sheet 2.
  • the side walls 42b of the container are delimited on the side of the cylinder by a circular line 42bi, which is extended to the upper part of the container by a straight line 42b 2 .
  • this straight line 42b 2 is applied against the flexible sheet 2, which seals the container at this location where the mixture, in the liquid state, begins its expansion.
  • the device comprises, inside the container and against the internal faces of the side walls 42b, against plates 44 which have the function of masking the vacuum existing between the side walls 42b and the flexible sheet 2, as illustrated in particular in FIG. 8 of the drawing.
  • the counter plates 44 have a fixed position relative to the cylinder 40 and include means for being adjusted and fixed at a determined position relative to the side walls 42b of the container. They have a circular edge 44a extended by a straight part 44b, so as to cooperate closely with the flexible sheet 2. They take the form of a curved strip with parallel lateral edges whose width is greater than the maximum space E left in line with the side walls 42b of the container.
  • the device described in FIGS. 8 and 9 may include a source supply in the side walls 42b of the container or by means of a dispensing head located above the container. . Also the side walls 42b can be brought closer or further apart from one another in order to determine the width of the strip of foam to be obtained.
  • the temperature of the mixture of liquid reactants contained in the container can be controlled by admitting into the cylinder a heat transfer liquid circulating in longitudinal conduits as has been described with reference to FIG. 3.
  • the casting head shown in Figures 8 and 9, allows the reaction mixture to flow in the liquid state, outside the container, 4 u right of the tray 5, the extension foam forming on the plate 5 to end on the conveyor 1.
  • FIG. 1 of the drawing in which the evolution of the mixture of reactants flowing in the liquid phase at station A and which, entering into reaction, develops progressively along a regular slope is schematically illustrated.
  • point B the final structure of a strip of foam.
  • the sheet of paper 46 from a roll 47 located in front of and above the cylinder casting head 4 extends in a vertical plane first in a direction inclined up and down to the sheet 2 carried by the plate 5.
  • the sheet 46 is then folded around a member 1b constituted by a very thick wall, the lower edge lc of which is straight and extends parallel by adjoining said sheet 2, so that the parts 46a and 46b move in parallel planes.
  • the part 46b is thus inclined from bottom to top and is wound around a coil 48 situated above the shaping device for the strips of foam, which is constituted by the horizontal sheet 2 and by the two sheets 6 delimiting the side walls of the conveyor.
  • the inclination of the part 46b is substantially that of the material 49 during development.
  • Part 46a of sheet 46 is located, relative to the U-shaped corridor of the conveyor, behind part 46b which is in contact with the foam. This continues its race in the strip state, being guided by the side sheets 6 until complete gelation.
  • FIG. 10 of the drawing illustrates a device according to the invention for manufacturing rigid foam panels.
  • This consists of a horizontal conveyor belt 50 extending in a horizontal plane above which is disposed a second conveyor 51.
  • the two conveyors 50/51 are parallel to each other and are spaced apart from the another of a distance d which corresponds to the thickness of the plate to be obtained.
  • the lower strand 51a of the conveyor 51 is covered with a sheet, for example of paper 52 from a reel 53 located in before and above the device.
  • the cylinder casting head 54 which is of the type described with reference to FIGS. 3 to 7, is mounted on a carriage 55 guided by rails 56.
  • the carrying strand 50a of the lower conveyor 50 is covered by a sheet of paper 57, which from a supply reel is supported on a roller 58 and passed into the casting head 54 partially surrounding the front cylinder 54a of the latter.
  • the distance separating the casting head 54 from the lower conveyor 50 is filled by a plate 59 made up of two telescopic parts 59a / 59b.
  • Each of these parts is constituted by a thin metal plate preferably made of copper or aluminum, which are adjacent and superimposed so as to be able to slide relative to each other according to the position of the casting head 54 by report to the conveyors.
  • the length of the plate 59 can thus be modified in a proportion close to 1 to 2 in order to determine a zone of expansion of the mixture and to control its expansion, the heating being ensured by a battery of transmitters with infrared 60 in position. adjustable and whose distribution is determined by the chosen zone length.
  • bars 61 are arranged parallel to the direction of movement of the conveyors 50/51. These bars are of a section less than 1 'thickness of the panels and extend horizontally in the middle of the space d existing between the conveyors 50/51.
  • the device comprises several bars 61 parallel to each other, which are located in the same plane.
  • the bars 61 are fixed to the structure of the machine to supports 62, situated at one of their ends and extending in a cantilever above the casting head 54 and between said conveyors 50/51 of such so their. free end is located substantially at the point where the foam takes its consistency.
  • Said bars constitute the cores around which sheaths 63 are formed, obtained from strips of paper 64 or polyethylene film for example, continuously folded by means of conical forming rollers 65 according to a known principle.
  • each bar 61 Upstream of each bar 61, is disposed a roller 66 on which the sheet 64 is supported from below.
  • the roller 66 is arranged so that the sheet comes to tangent the bar 61 at its lower part. This is of a reduced section and profiled at its part 61a to accompany the sheet 64 before it is brought into contact with the forming rollers 65. These are arranged so as to bring one of the edges of the sheet into overlap on the other, as illustrated in FIG. 12.
  • the sheath thus formed at the level of station A is closed by gluing or by welding by means of two knobs 67 which apply the edges to each other.
  • the sheaths are driven at the same speed as the conveyors 50/51 initially by means of a clamping device and then by the material itself by adhesion of the latter to the sheaths.
  • the foam in formation develops around the sheaths 63 between the conveyors 50/51 until total expansion
  • the panel obtained at the outlet of the conveyors comprises parallel longitudinal channels between them and delimited by said sheaths.
  • a panel thus obtained is illustrated in Figure 13 of the drawing.
  • the layer of foam 68 calibrated in thickness between the two conveyors 50/51 is protected on the large faces of the panel by sheets of paper 52/57.
  • the channels 69 formed by the cores 61 adopt the shape of the latter and extend in the longitudinal direction of the panel.
  • the example shown comprises channels 69 of a circular cross section, the peripheral wall of which is delimited and protected by the sheaths 63 which adhere to the foam.
  • the sheaths-63 can also be constituted by rigid tubes made of cardboard or plastic.

Landscapes

  • Casting Or Compression Moulding Of Plastics Or The Like (AREA)
  • Manufacture Of Porous Articles, And Recovery And Treatment Of Waste Products (AREA)
  • Laminated Bodies (AREA)
  • Materials For Medical Uses (AREA)

Abstract

PCT No. PCT/FR82/00056 Sec. 371 Date Nov. 1, 1982 Sec. 102(e) Date Nov. 1, 1982 PCT Filed Mar. 23, 1982 PCT Pub. No. WO82/03357 PCT Pub. Date Oct. 14, 1982.An apparatus for manufacturing continuous webs of polymer foam obtained from a mixture of liquid reagents, wherein the volume of a container is determined to form a zone of retention of the mixture of reagents in liquid phase and wherein the level of this mixture is maintained at a level slightly higher than the plane upon which the mixture in the liquid state flows, so that the primary phase of expansion of the mixture and its further expansion are produced outside the container on a moving surface of the conveyor, which surface is maintained in a substantially horizontal plane. The invention is particularly applicable to the production of webs of supple foam or of panels of rigid foam.

Description

La présente invention a pour objet un procédé et un dispositif pour fabriquer des bandes de mousse de polymères et produit obtenu.The present invention relates to a method and a device for manufacturing strips of polymer foam and product obtained.

Le secteur technique de l'invention est celui des appareillages pour la mise en oeuvre de bandes de mousse souple ou rigide.The technical sector of the invention is that of equipment for the implementation of flexible or rigid foam strips.

On sait que dans le processus de moussage polyuréthane, deux réactions simultanées se produisent entre d'une part l'isocyanate et le polyol (ou polyalcool) et d'autre part entre l'isocyanate et l'eau, qui produit le principal agent d'expansion : le gaz carbonique. Cette dernière réaction éventuellement combinée au phénomène physique de l'ébullition d'un agent gonflant auxiliaire (chlorure de méthylène ou trichlo- rofluométhane) provoque l'expansion de la mousse. On obtient ainsi un matériau poreux thermodurcissable qui peut être, soit souple, soit rigide selon le.degré de réticulation du palymère.It is known that in the polyurethane foaming process, two simultaneous reactions occur between on the one hand the isocyanate and the polyol (or polyalcohol) and on the other hand between the isocyanate and the water, which produces the main agent of 'expansion: carbon dioxide. This last reaction, possibly combined with the physical phenomenon of the boiling of an auxiliary swelling agent (methylene chloride or trichlorofluomethane) causes the foam to expand. A porous thermosetting material is thus obtained which can be either flexible or rigid depending on the degree of crosslinking of the palymer.

Les procédés de coulée en continue actuellement connus consistent, pour la plupart, à répartir aussi uniformément que possible le mélange réactif liquide sur la largeur d'un convoyeur incliné, formé d'un fond et-de deux parois latérales qui se déplacent perpendiculairement à la répartition du liquide. Cette répartition d'un mélange de réactants liquides, peu visqueux, et de réactivité rapide, implique une zone de rétention capable de contenir le liquide déversé pendant le temps nécessaire et suffisant à cette opération. Dans cette conception, l'inclinaison du convoyeur est généralement de 4 à 6° sur la longueur nécessaire à l'expansion de la mousse et à sa gélification : entre quinze et vingt mètres. Le déplacement s'effectue ensuite sur un plan horizontal jusqu'à l'équipement de coupe transversal : environ cinquante mètres du point de coulée.The currently known continuous casting methods consist, for the most part, in distributing the liquid reactive mixture as uniformly as possible over the width of an inclined conveyor, formed by a bottom and by two side walls which move perpendicular to the liquid distribution. This distribution of a mixture of liquid reactants, which is not very viscous, and of rapid reactivity, implies a retention zone capable of containing the liquid spilled for the time necessary and sufficient for this operation. In this design, the inclination of the conveyor is generally 4 to 6 ° over the length necessary for the expansion of the foam and its gelation: between fifteen and twenty meters. The movement is then made on a horizontal plane to the cross cutting equipment: about fifty meters from the casting point.

Les dispositifs les plus classiques comportent une tête de coulée animée d'un mouvement transversal de va et vient et la zone de rétention des réactants est formée, en amont par le fond du convoyeur, généralement constitué par une feuille de matériau souple : feuille de papier ou de polyéthylène, latéralement par des parois à défilement continu constituées par le même matériau que celui du fond et en aval, par le produit lui-même qui entre dans sa phase réactive initiale dite "ligne de crème". On précise que l'expression "ligne de crème" désigne l'état du mélange des réactants survenant immédiatement après la phase liquide- et dans lequel ce mélange atteint une grande viscovité précédant la formation de la mousse. Le produit à l'état visqueux adhère au support de fond et constitue, constamment renouvelé, un barrage à l'écoulement du mélange liquide le long de la pente du convoyeur. Afin de compenser l'absence de mélange dans cet état, on place, au commencement de la fabrication, un obstacle en aval de la tête de coulée, dont le rôle est de retenir le mélange liquide au démarrage.The most conventional devices include a casting head animated with a transverse movement back and forth and the reactant retention zone is formed, upstream by the bottom of the conveyor, generally consisting of a sheet of flexible material: sheet of paper or of polyethylene, laterally by continuously scrolling walls made of the same material as that of the bottom and downstream, by the product itself which enters its initial reactive phase called "cream line". It is specified that the expression "cream line" designates the state of the mixture of reactants occurring immediately after the liquid phase - and in which this mixture reaches a high viscosity. preceding the formation of the foam. The viscous product adheres to the bottom support and constitutes, constantly renewed, a barrier to the flow of the liquid mixture along the slope of the conveyor. In order to compensate for the absence of mixing in this state, an obstacle is placed downstream of the casting head at the start of manufacture, the role of which is to retain the liquid mixture at start-up.

Sur ce principe, on connaît un procédé décrit dans le brevet français 1 579 795 selon lequel on place sous le support souple, un élément transversal d'un profil déterminé pour imprimer un mouvement ascendant dudit support sur une très courte distance et ainsi former la paroi aval de la zone de rétention. Ce procédé permet d'améliorer la répartition du mélange liquide sur la largeur du convoyeur et de réduire, voire même supprimer le mouvement de va et vient de la tête de coulée.On this principle, there is a process described in French patent 1,579,795 according to which a transverse element of a determined profile is placed under the flexible support to impart an upward movement of said support over a very short distance and thus form the wall. downstream of the retention zone. This process makes it possible to improve the distribution of the liquid mixture over the width of the conveyor and to reduce, or even eliminate the back and forth movement of the casting head.

Ce principe est également appliqué dans le procédé décrit dans le brevet français 72 76616 selon lequel on utilise une barre cylindrique protégée par un support souple supérieur, par exemple une bande de papier, qui lamine le mélange liquide au point précis de la ligne de crème, créant ainsi, par un réglage approprié à chaque fabrication et constamment surveillé, un équilibre fragile entre l'arrivée de liquide et son évacuation dans la zone d'expansion. Selon ce procédé, la paroi aval est formée par la barre cylindrique en combinaison avec la ligne de crème qui la suit immédiatement.This principle is also applied in the method described in French patent 72 76616 according to which a cylindrical bar is used protected by an upper flexible support, for example a strip of paper, which laminates the liquid mixture at the precise point of the cream line, thus creating, by an adjustment appropriate to each production and constantly monitored, a fragile balance between the arrival of liquid and its evacuation in the expansion zone. According to this method, the downstream wall is formed by the cylindrical bar in combination with the line of cream which immediately follows it.

Un autre procédé connu est décrit dans le brevet français 71 31528, lequel consiste à répartir le.mélange liquide sur le convoyeur par l'intermédiaire d'un récipient ou auge, dans lequel les réaetants sont introduits par le fond et où leur expansion commence à se produire. Les réactants, à l'état de mousse naissante, débordent de ce récipient pour se déverser sur le convoyeur.Another known method is described in French patent 71 31528, which consists in distributing the liquid mixture on the conveyor by means of a container or trough, in which the reagents are introduced from the bottom and where their expansion begins to happen. The reactants, in the form of nascent foam, overflow from this container to pour onto the conveyor.

Tous ces procédés et dispositifs connus présentent des inconvénients.All of these known methods and devices have drawbacks.

Dans les trois premiers procédés susmentionnés, la paroi amont est toujours formée par le fond du convoyeur qui doit nécessairement être incliné. Le principal inconvénient, découlant de cette conception, est la difficulté de maîtriser l'écoulement parasitaire de la phase liquide des réactants, sous la ligne,de crème.In the first three processes mentioned above, the upstream wall is always formed by the bottom of the conveyor which must necessarily be inclined. The main drawback, arising from this design, is the difficulty of controlling the parasitic flow of the liquid phase of the reactants, below the line, of cream.

. Les inconvénients du dernier procédé cité plus haut sont les suivants : .

  • a) -la zone de rétention, constituée par un récipient statique est sujette à un encrassement continuel inévitable en raison de la nature évolutive du mélange;
  • b)- la capacité du récipient ne pouvant être modifiée en cours de fabrication, la réactivité du mélange doit par conséquent, être lente sans possibilité de l'adapter aux autres impératifs;
  • c)- le volume de matière, relativement important, contenu dans le récipient et le fait que la réaction commence à s'y déclencher, sont des facteurs d'élévation progressive de la température dans ledit récipient, ce qui modifie l'évolution de la transformation du mélange réactif;
  • d)- les écoulements parasitaires sous la mousse en expansion ne sont pas totalement éliminés en raison de l'utilisation d'un convoyeur incliné.
. The disadvantages of the last process mentioned above are the following:.
  • a) -the retention zone, consisting of a static container is subject to inevitable continual fouling due to the evolving nature of the mixture;
  • b) - the capacity of the container cannot be modified during manufacture, the reactivity of the mixture must therefore be slow without the possibility of adapting it to other requirements;
  • c) - the relatively large volume of material contained in the container and the fact that the reaction begins to start there, are factors of progressive rise in temperature in said container, which modifies the evolution of the transformation of the reactive mixture;
  • d) - parasitic flows under the expanding foam are not completely eliminated due to the use of an inclined conveyor.

Tel que cela vient d'être exposé, le mélange,pendant son expansion, passe progressivement de l'état liquide à l'état solide, le produit fini pouvant être rigide ou souple en fonction du degré de réticulation du polymère. L'état rapidement visqueux puis pâteux du mélange provoque contre les parois du conformateur quel qu'il soit : un moule fermé ou ouvert sur le dessus, une retenue qui freine l'expansion des cellules venant au contact des parois.As has just been exposed, the mixture, during its expansion, progressively passes from the liquid state to the solid state, the finished product being able to be rigid or flexible depending on the degree of crosslinking of the polymer. The rapidly viscous then pasty state of the mixture causes against the walls of the shaper whatever it is: a closed or open mold on top, a retainer which slows down the expansion of the cells coming into contact with the walls.

Dans le cadre de la production de blocs ou de bandes d'une section droite rectangulaire notamment, il résulte de ce phénomène, une forme arrondie de la face supérieure du bloc de mousse à la fin de l'expansion. Cette forme est à l'origine de pertes de matière importantes lors de la fabrication de tels blocs ou bandes.In the context of the production of blocks or strips of a rectangular cross section in particular, it results from this phenomenon, a rounded shape of the upper face of the foam block at the end of the expansion. This shape is the source of significant material losses during the manufacture of such blocks or strips.

On a donc cherché à donner à la section des blocs coulés en continu une forme aussi rectangulaire que possible.We therefore sought to give the section of continuously cast blocks as rectangular as possible.

Un procédé et un dispositif connus consistent à doubler les parois mobiles latérales avec un film dé polyéthylène tiré d'abord suivant un angle déterminé jusqu'au point d'achèvement de l'expansion de la mousse d'où, après formation d'un pli, il accompagne ensuite le bloc de mousse jusqu'à la sortie du convoyeur.A known method and device consists in lining the lateral movable walls with a polyethylene film drawn first at a determined angle to the point of completion of the expansion of the foam, from which, after forming a fold , it then accompanies the foam block until it leaves the conveyor.

Selon un autre procédé, on comprime la mousse en formation à l'aide de patins lestés en appui sur la face supérieure du bloc , par l'intermédiaire d'une bande de papier ou d'une bande de fibre non tissée, qui accompagne le bloc lors de son déplacement sur le convoyeur.According to another method, the foam in formation is compressed using weighted pads bearing on the upper face of the block, by means of a strip of paper or a strip of non-woven fiber, which accompanies the block when moving on the conveyor.

Un autre procédé décrit dans le brevet français 71 31528 consiste à placer le point de coulée sensiblement à la même altitude que la face supérieure du bloc à obtenir et on assure l'expansion de la mousse par l'inclinaison contrôlée du convoyeur.Another process described in French patent 71 31528 consists in placing the pouring point at substantially the same altitude as the upper face of the block to be obtained and the foam is expanded by the controlled inclination of the conveyor.

Ces trois procédés présentent des inconvénients.These three methods have drawbacks.

Les inconvénients du premier procédé résident dans le fait qu'il nécessite l'utilisation de feuilles d'un matériau très souple en vue de sa déformabilité. Un tel matériau, de préférence le polyéthylène, est relativement fragile et actuellement onéreux puisqu'il s'agit d'un dérivé du pétrole.The drawbacks of the first method lie in the fact that it requires the use of sheets of a very flexible material with a view to its deformability. Such a material, preferably polyethylene, is relatively fragile and currently expensive since it is a petroleum derivative.

D'autre part, le pli formé au point final de l'expansion de la mousse laisse dans les faces latérales des bandes, des traces- qui obligent à un dressage des flancs, ce qui entraîne des perces de matière importantes.On the other hand, the fold formed at the end point of the expansion of the foam leaves traces on the lateral faces of the strips, which make it necessary to straighten the flanks, which results in significant material piercing.

Les inconvénients du deuxième procédé sont tout d'abord qu'il nécessite un appareillage complexe et de réglage délicat. De plus, toute variation de la ligne de crème est génératrice d'inclusion d'air entre la bande de papier et la face supérieure du bloc, laquelle présente alors des criques en profondeur, parfois importantes, ce qui entraîne la perte d'une partie de la bande. Egalement selon ce procédé, le papier supérieur ne peut être retiré qu'après gélification totale du bloc, c'est-à-dire vingt-cinq à trente mètres après la coulée et en conséquence les défauts ne sont visibles par les opérateurs qu'à partir de ce moment, ce qui entraîne un retard considérable dans les manoeuvres correctives.The disadvantages of the second method are first of all that it requires complex apparatus and delicate adjustment. In addition, any variation in the cream line generates air inclusion between the paper strip and the upper face of the block, which then has deep, sometimes significant cracks, which results in the loss of part Of the band. Also according to this process, the upper paper can only be removed after total gelation of the block, that is to say twenty-five to thirty meters after casting and consequently the defects are only visible to the operators from this moment, which causes a considerable delay in corrective maneuvers.

L'inconvénient du troisième procédé réside dans la complexité du dispositif de variation de largeur de la bande de mousse en cours de fabrication.The drawback of the third method lies in the complexity of the device for varying the width of the strip of foam during manufacture.

Les plaques de mousse rigide, d'épaisseur contrôlée et dont chaque face est constituée par un matériau de protection : papier, tissu, plaque de plâtre, bois etc ... sont généralement fabriquées en continu, en largeur standard de préférence d'un mètre vingt centimètres, au moyen de convoyeurs horizontaux dits à double bande, dont l'un inférieur supporte une bande qui reçoit le mélange réactif et l'autre supérieur comporte une bande qui limite l'expansion du produit et assure outre le calibrage, la planéité de la face supérieure.The rigid foam sheets, of controlled thickness and each side of which is made up of a protective material: paper, fabric, plasterboard, wood, etc. are generally manufactured continuously, in standard width preferably one meter. twenty centimeters, by means of horizontal conveyors known as double belts, one lower of which supports a band which receives the reactive mixture and the other upper comprises a band which limits the expansion of the product and ensures, in addition to sizing, the flatness of the upper side.

Dans ce type de fabrication, il est utile de pouvoir ajuster la distance entre le point de coulée, ou zone de rétention, et l'entrée du mélangé en cours d'expansion sous le convoyeur supérieur. De même, il est nécessaire de contrôler la température du support flexible inférieur dans la partie précédant l'entrée du mélange dans le passage existant entre le convoyeur supérieur et le convoyeur inférieur.In this type of manufacturing, it is useful to be able to adjust the distance between the pour point, or retention zone, and the entry of the mixture being expanded under the upper conveyor. Likewise, it is necessary to control the temperature of the lower flexible support in the part preceding the entry of the mixture into the passage existing between the upper conveyor and the lower conveyor.

Un objectif de l'invention consiste en la mise en oeuvre de moyens pour la fabrication de bandes de polymères souples ou rigides et permettant :

  • - d'obtenir une zone de rétention délimitée avec précision par les éléments mécaniques du dispositif;
  • - de contrôler, faire varier et ajuster le volume de ladite zone selon les caractéristiques du mélange réactif et du produit à fabriquer;
  • - d'utiliser à ces fins une combinaison d'éléments ayant entre eux un mouvement relatif continu et dont le sens est déterminé de telle sorte que le mélange en phase liquide soit maintenu dans cette zone, sans fuite appréciable, pour s'écouler ensuite naturellement sur le convoyeur dont l'extrémité amont constitue une paroi de la zone de rétention;
  • - de régler les altitudes et mouvements respectifs des appareils de telle sorte que l'écoulement du mélange liquide ne soit possible que dans la direction du convoyeur sans qu'il soit nécessaire d'incliner celui-ci.
An objective of the invention consists in the implementation of means for the manufacture of flexible or rigid polymer strips and allowing:
  • - to obtain a retention zone delimited with precision by the mechanical elements of the device;
  • - controlling, varying and adjusting the volume of said zone according to the characteristics of the reactive mixture and of the product to be manufactured;
  • - to use for these purposes a combination of elements having between them a continuous relative movement and whose direction is determined so that the liquid phase mixture is maintained in this zone, without appreciable leakage, to then flow naturally on the conveyor, the upstream end of which forms a wall of the retention zone;
  • - to adjust the respective altitudes and movements of the devices so that the flow of the liquid mixture is only possible in the direction of the conveyor without it being necessary to tilt it.

Un autre objectif de l'invention est de réaliser des bandes de mousse de polymères souples d'une section droite rectangulaire dont la face supérieure est plane.Another objective of the invention is to produce strips of flexible polymer foam with a rectangular cross section whose upper face is flat.

Un autre objectif de l'invention est la fabrication de plaques de mousse rigide chargée et/ou allégée, notamment des plaques comportant dans leur épaisseur des canaux longitudinaux et parallèles entre eux alors que les techniques actuellement connues ne permettent que la production de panneaux pleins en matière vierge.Another objective of the invention is the manufacture of rigid foam plates loaded and / or lightened, in particular plates having in their thickness longitudinal and parallel channels between them while the currently known techniques only allow the production of solid panels in virgin matter.

Ces objectifs sont atteints par le procédé selon l'invention pour la fabrication de bandes continues de mousse de polymères obtenues à partir d'un mélange de réàctants liquides, générateurs d'une mousse expansée, selon lequel on introduit en continu ledit mélange de réac- . tants liquides dans un récipient et en ce qu'on laisse le mélange se dilater de telle sortie qu'une fois totalement expansée, la mousse prise en charge par un convoyeur en U, animé d'un mouvement continu adopte la forme d'une bande de section droite rectangulaire, caractérisé en ce qu'on détermine le volume dudit récipient pour former une zone de rétention du mélange de réactants en phase liquide et en ce que l'on maintient le niveau de ce mélange à un niveau légèrement supérieur au plan sur lequel s'écoule le mélange à l'état liquide, de telle sorte que la phase primaire de la dilatation du mélange et son expansion se produisent à l'extérieur du récipient sur une surface animée d'un mouvement continu sous l'effet du convoyeur, laquelle surface est maintenue dans un plan sensiblement horizontal.These objectives are achieved by the process according to the invention for the production of continuous strips of polymer foam obtained from a mixture of liquid reactants, generators of expanded foam, according to which said mixture of reactants is continuously introduced. . liquid in a container and in that the mixture is allowed to expand at such an outlet that once fully expanded, the foam supported by a U-shaped conveyor, animated in a continuous movement takes the form of a band of rectangular cross section, characterized in that the volume of said container is determined to form a zone of retention of the mixture of reactants in the liquid phase and in that the level of this mixture is maintained at a level slightly higher than the plane over which the mixture flows in the liquid state, so that the primary phase of the expansion of the mixture and its expansion occur outside the container on a surface animated by a continuous movement under the effect of the conveyor, which surface is maintained in a substantially horizontal plane.

Le volume du récipient est notamment déterminé en intervenant sur au moins sa longueur, de telle sorte que la zone de rétention définisse la largeur de la bande de mousse.The volume of the container is in particular determined by operating over at least its length, so that the retention zone defines the width of the foam strip.

Ces objectifs sont également atteints par le dispositif selon l'invention pour réaliser des bandes de mousse de polymères obtenues à partir d'un mélange de réactants liquides générateurs d'une mousse expansée et comportant un récipient, des moyens pour introduire en continu dans ce récipient, ledit mélange de réactants liquides et un convoyeur en U, animé d'un mouvement continu sur lequel la mousse est déposée pour adopter la forme d'une bande d'une section droite rectangulaire, caractérisé en ce que le récipient comporte une paroi avant, une paroi arrière et deux parois latérales dont les parois avant et arrière constituent également le fond du récipient et en ce que la paroi avant, qui est située du côté du convoyeur est une paroi courbe constituée par un cylindre, animé en rotation autour d'un axe sensiblement horizontal dans le même sens et à la même vitesse que le convoyeur et en ce que les bords des parois latérales, situées du côté de la paroi courbe,sont d'un contour circulaire et entourent partiellement le.cy- lindre afin de permettre le mouvement relatif du cylindre et des autres parois tout en assurant l'étanchéité du récipient.These objectives are also achieved by the device according to the invention for producing strips of polymer foam obtained from a mixture of liquid reactants generating an expanded foam and comprising a container, means for continuously introducing into this container , said mixture of liquid reactants and a U-shaped conveyor, animated by a continuous movement on which the foam is deposited to take the form of a strip of a rectangular cross section, characterized in that the container has a front wall, a rear wall and two side walls, the front and rear walls of which also constitute the bottom of the container and in that the front wall, which is situated on the side of the conveyor, is a curved wall constituted by a cylinder, driven in rotation around a axis substantially horizontal in the same direction and at the same speed as the conveyor and in that the edges of the side walls, located on the side of the curved wall, are of a circular outline and partially surround the cylinder in order to allow the relative movement of the cylinder and of the other walls while ensuring the sealing of the container.

Le bord supérieur de la paroi arrière et des parois latérales du récipient se situent à un niveau supérieur à celui de la paroi avant, laquelle tangente une surface sensiblement horizontale sur laquelle s'écoule le mélange de réactants en phase liquide, laquelle surface horizontale est animée d'un mouvement continu sous l'effet du convoyeur.The upper edge of the rear wall and the side walls of the container are located at a level higher than that of the front wall, which tangents a substantially horizontal surface over which the mixture of reactants in liquid phase flows, which horizontal surface is animated. of a continuous movement under the effect of the conveyor.

L'ensemble : parai arrière, parois latérales, comporte des moyens pour obtenir son pivotement autour de l'axe dudit cylindre dans le but d'élever ou'd'abàisser ledit ensemble par rapport à ladite surface horizontale afin de modifier le volume du récipient; et pour immobiliser en position ledit ensemble après réglage.The assembly: rear wall, side walls, includes means for obtaining its pivoting around the axis of said cylinder in order to raise or lower said assembly relative to said horizontal surface in order to modify the volume of the container. ; and to immobilize in position said assembly after adjustment.

Selon un mode de réalisation, la paroi arrière du récipient est une paroi courbe constituée par un cylindre, entraîné en rotation dans le même sens que le cylindre avant, lesquels cylindres sont montés sur deux axes parallèles entre eux et sont sensiblement tangents, la ligne de tangence constituant le fond du récipient et en ce que les parois latérales sont parallèles entre elles et sont au-dessus des cylindres et leur bord inférieur est délimité par deux lignes circulaires concourantes en un point situé au voisinage de ladite ligne de tangence, lesquelles parois latérales entourent partiellement les cylindres afin de permettre d'une part la rotation des cylindres et d'autre part le mouvement relatif de l'ensemble cylindre arrière/parois latérales autour du cylindre avant tout en assurant l'étanchéité du récipient.According to one embodiment, the rear wall of the container is a curved wall formed by a cylinder, driven in rotation in the same direction as the front cylinder, which cylinders are mounted on two axes parallel to each other and are substantially tangent, the line of tangency constituting the bottom of the container and in that the side walls are parallel to each other and are above the cylinders and their lower edge is delimited by two concurrent circular lines at a point located in the vicinity of said line of tangency, which side walls partially surround the cylinders in order to allow on the one hand the rotation of the cylinders and on the other hand the relative movement of the rear cylinder / side walls assembly around the front cylinder while ensuring the tightness of the container.

Le cylindre arrière est d'un diamètre plus grand que le cylindre avant et est entraîné en rotation à une vitesse plus lente que celle dudit cylindre avant.The rear cylinder has a larger diameter than the front cylinder and is rotated at a slower speed than that of said front cylinder.

. Le cylindre arrière est plongé dans un bac à solvant et est soumis à l'action d'une raclette s'étendant dans le sens longitudinal du cylindre pour décoller à sa périphérie les particules polymérisées y adhérant.. The rear cylinder is immersed in a solvent tank and is subjected to the action of a squeegee extending in the longitudinal direction of the cylinder to detach the polymerized particles adhering thereto at its periphery.

Chacune des parois latérales comporte une contre-plaque s'étendant du côté de ladite surface horizontale sur laquelle est déposé le mélange de réactants en phase liquide pour réaliser l'étanchéité à la jonction des parois latérales et de ladite surface, lesquelles contre-plaques sont réglables en position sur les parois.Each of the side walls has a counter plate extending from the side of said horizontal surface on which the mixture of reactants in the liquid phase is deposited to seal at the junction of the side walls and said surface, which counter plates are adjustable in position on the walls.

Lesdites parois latérales comportent des moyens pour les rapprocher l'une vers l'autre ou les éloigner l'une dé l'autre et pour les immobiliser en position.Said side walls include means for bringing them towards one another or away from one another and for immobilizing them in position.

Au moins un desdits cylindres comporte un faisceau de conduits parallèles entre eux et à l'axe de rotation du cylindre, dans lesquels conduits est mis en circulation un fluide caloporteur pour élever ou abaisser la température du cylindre et corrélativement la température du mélange de réactants en phase liquide.At least one of said cylinders comprises a bundle of conduits which are parallel to each other and to the axis of rotation of the cylinder, in which conduits a coolant is circulated in order to raise or lower the temperature of the cylinder and correspondingly the temperature of the mixture of reactants in liquid phase.

La paroi courbe constituée par ledit cylindre, située a l'avant du récipient du côté du convoyeur et la paroi arrière du récipient, définissent un espace dans lequel est passée une feuille souple, laquelle s'enroule partiellement autour dudit cylindre sur lequel elle se déplace dans le récipient, laquelle feuille poursuit sa course en étant prise en charge par le convoyeur et constitue ladite surface horizontale sur laquelle est déposé le mélange de réactants.The curved wall formed by said cylinder, located at the front of the container on the side of the conveyor and the rear wall of the container, define a space in which a flexible sheet has passed, which partially wraps around said cylinder on which it moves. in the container, which sheet continues to run while being supported by the conveyor and constitutes said horizontal surface on which the mixture of reactants is deposited.

Dans un mode de réalisation, la feuille souple est appliquée contre la partie inférieure dudit cylindre avant, au-dessous. du fond du récipient, au moyen d'un rouleau soumis à l'action de moyens élastiques.In one embodiment, the flexible sheet is applied against the lower part of said front cylinder, below. from the bottom of the container, by means of a roller subjected to the action of elastic means.

Dans un autre mode de réalisation, la feuille souple est appliquée contre la partie inférieure du cylindre arrière, au-dessous de la ligne de tangence des deux cylindres au moyen d'un rouleau soumis à l'action de moyens élastiques, laquelle feuille est ensuite passée entre les deux cylindres et entoure partiellement le cylindre avant par le dessus pour s'étendre tangentiellement à celui-ci dans une position sensiblement horizontale.In another embodiment, the flexible sheet is applied against the lower part of the rear cylinder, below the line of tangency of the two cylinders by means of a roller subjected to the action of elastic means, which sheet is then passed between the two cylinders and partially surrounds the front cylinder from above to extend tangentially thereto in a substantially horizontal position.

Dans le dispositif selon l'invention dont le mélange est introduit en source dans le récipient, une caractéristique est qu'il comporte au moins une tubulure traversant chacune des parois. latérales, laquelle tubulure est montée coulissante pour être positionnée dans la tête de coulée et comporte sur sa longueur des ouvertures pour assurer la répartition du mélange à l'état liquide dans ladite tête.In the device according to the invention, the mixture of which is introduced at the source into the container, a characteristic is that it comprises at least one tube passing through each of the walls. lateral, which tubing is slidably mounted to be positioned in the casting head and has along its length openings to ensure the distribution of the mixture in the liquid state in said head.

Dans un mode particulier de réalisation, la tubulure se compose de plusieurs tubes coaxiaux, disposés dans le prolongement l'un de l'autre et de section dégressive par rapport à la circulation du mélange, de telle sorte à réserver entre eux des espaces annulaires sensiblement de même section, laquelle correspond approximativement à la section du plus petit tube central.In a particular embodiment, the tubing consists of several coaxial tubes, arranged in the extension of one another and of tapering section with respect to the circulation of the mixture, so as to reserve between them substantially annular spaces of the same section, which corresponds approximately to the section of the smallest central tube.

Le dispositif selon l'invention comporte également un plateau sensiblement horizontal, d'une largeur au moins égale à celle du convoyeur et dont la face supérieure est tangente au cylindre avant du récipient, lequel'plateau s'étend dudit cylindre avant jus- .qu'au convoyeur et supporte la feuille sur laquelle se développe la mousse.The device according to the invention also comprises a substantially horizontal plate, of a width at least equal to that of the conveyor and the upper face of which is tangent to the front cylinder of the container, which tray extends from said front cylinder to. 'to the conveyor and supports the sheet on which the foam develops.

Dans ledit dispositif, dans lequel le convoyeur en U se compose d'un tapis porteur de la feuille souple sur laquelle se développe la mousse et dont les parois latérales sont constituées par deux feuilles souples, chacune issue d'un rouleau vertical situé à l'avant du dispositif du côté du récipient, lesquelles feuilles s'étendent sur la longueur du convoyeur et s'enroulent autour d'un rouleau vertical situé à l'arrière du dispositif, lesdites feuilles se déplaçant à la vitesse du tapis en étant accolées du côté de leur bord inférieur le long des bords latéraux de ladite feuille, portée par le convoyeur, une caractéristique consiste dans le fait qu'il comporte en outre parallèlement et à proximité de chacune des faces internes des parois latérales du convoyeur, une autre feuille souple inclinée, laquelle issue d'un.rouleau situé du côté dudit récipient, s'étend sur au moins la partie du dispositif où les réactants déposés en phase liquide sur ladite feuille horizontale entrent en réaction et se développent jusqu'à l'expansion totale de la mousse, laquelle feuille se déplace dans cette partie suivant une direction rectiligne de l'entrée vers la sortie du dispositif et dé bas en haut pour être prise en charge par un rouleau situé au-dessus du convoyeur, son inclinaison étant telle que ses bords latéraux sont sensiblement parallèles à la pente du mélange en phase de réaction afin d'obtenir des bandes de mousse ayant une face supérieure plane formant avec leurs faces latérales des arêtes vives exemptes de défaut de surface.In said device, in which the U-shaped conveyor consists of a mat carrying the flexible sheet on which the foam develops and whose side walls are constituted by two flexible sheets, each from a vertical roller located at the front of the device on the container side, which sheets extend over the length of the conveyor and are wound around a vertical roller situated at the rear of the device, said sheets moving at the speed of the mat while being attached to the side of their lower edge along the lateral edges of said sheet, carried by the conveyor, a characteristic consists in the fact that it furthermore comprises parallel and close to each of the internal faces from the side walls of the conveyor, another inclined flexible sheet, which comes from a roll located on the side of said container, extends over at least the part of the device where the reactants deposited in liquid phase on said horizontal sheet enter into reaction and develop until the total expansion of the foam, which sheet moves in this part in a rectilinear direction from the inlet to the outlet of the device and from the bottom up to be supported by a roller located above of the conveyor, its inclination being such that its lateral edges are substantially parallel to the slope of the mixture in the reaction phase in order to obtain strips of foam having an upper face pla forming with their lateral faces sharp edges free from surface defects.

Les parties inclinées de ladite feuille sont situées au-dessus du convoyeur et de la tête de coulée et une des parties est inclinée de haut en bas et pliée le long d'un organe rectiligne parallèle et jouxtant la feuille horizontale et l'autre partie est renvoyée de bas en haut suivant la même inclinaison que celle de ladite première partie.The inclined parts of said sheet are located above the conveyor and the casting head and one of the parts is inclined up and down and folded along a parallel rectilinear member and adjoining the horizontal sheet and the other part is returned from bottom to top at the same inclination as that of said first part.

Dans sa conception pour la mise en oeuvre de panneaux en mousse rigide, le dispositif selon l'invention, comportant un convoyeur inférieur, porteur d'une feuille souple sur laquelle est déposé le mélange de réactants et un deuxième convoyeur disposé au-dessus dudit convoyeur inférieur et parallèle à celui-ci et sur lequel . est appliquée une feuille souple sur le brin inférieur du tapis supérieur, lesquels convoyeurs définissent un espace qui détermine l'épaisseur des panneaux de mousse rigide,se caractérise en ce que le récipient dans lequel sont introduits les réactants liquides est déplaçable dans le sens longitudinal du dispositif et comporte des moyens pour être immobilisé en position par rapport aux convoyeurs,In its design for the implementation of rigid foam panels, the device according to the invention, comprising a lower conveyor, carrying a flexible sheet on which the mixture of reactants is deposited and a second conveyor disposed above said conveyor lower and parallel to it and on which. is applied a flexible sheet on the lower strand of the upper mat, which conveyors define a space which determines the thickness of the rigid foam panels, is characterized in that the container in which the liquid reactants are introduced is movable in the longitudinal direction of the device and comprises means for being immobilized in position relative to the conveyors,

Dans ce mode de réalisation, le plateau,qui s'étend entre le récipient et le convoyeur inférieur, se compose d'au moins deux plaques de faible épaisseur, parallèles entre elles et adjacentes, lesquelles plaques sont télescopiques pour ajuster la longueur du plateau afin de-relier le récipient et le convoyeur.In this embodiment, the plate, which extends between the container and the lower conveyor, consists of at least two thin plates, mutually parallel and adjacent, which plates are telescopic to adjust the length of the plate so de-connect the container and the conveyor.

Ce dispositif comporte, dans l'espace existant entre le convoyeur inférieur et le convoyeur supérieur, des barreaux parallèles entre eux et disposés dans un même plan, lesquels barreaux sont en porte à faux et sont fixés à la structure du dispositif du côté dudit récipient et s'étendent vers les convoyeurs, de telle sorte que leur extrémité libre,qui se trouve entre lesdits convoyeurs, se situe sensiblement au lieu où se produit la solidification de la mousse.This device comprises, in the space existing between the lower conveyor and the upper conveyor, bars parallel to each other and arranged in the same plane, which bars are cantilevered and are fixed to the structure of the device on the side of said container and extend towards the conveyors, so that their free end, which is located between said conveyors, is located substantially at the place where the solidification of the foam occurs.

Chacun de ces barreaux est enveloppé par une gaine légèrement plus grande que le barreau pour pouvoir être déplacée le long de celui-ci sous l'effet de la mousse pendant son expansion afin de réaliser en continu et délimiter des canaux dans les panneaux de mousse.Each of these bars is surrounded by a sheath slightly larger than the bar so that it can be moved along the latter under the effect of the foam during its expansion in order to continuously produce and delimit channels in the foam panels.

L'invention concerne également un produit nouveau consistant en un panneau de mousse rigide dont les grandes faces sont recouvertes de feuilles d'un matériau de protection, se caractérisant en ce qu'il comporte, dans son épaisseur, des canaux parallèles entre eux dont la paroi périphérique est protégée par une gaine adhérant à la mousse.The invention also relates to a new product consisting of a rigid foam panel whose large faces are covered with sheets of protective material, characterized in that it comprises, in its thickness, parallel channels between them, the peripheral wall is protected by a sheath adhering to the foam.

Les avantages de l'invention se situent à divers niveaux.:

  • -elle est simple de conception et facile à adapter sur tous les types de machines de moussage;
  • - elle peut être utilisée aussi bien pour la fabrication de la mousse souple que pour la fabrication de la mousse rigide;
  • - elle offre la possibilité de faire varier la laize en continu;
  • - également la possibilité de faire varier en continu le volume du liquide en rétention avant le démarrage de la réaction de moussage ou, selon le besoin, la possibilité de conserver ce volume constant tout en changeant de laize : il'n'est donc pas nécessaire de faire un ajustement de catalyse;
  • - elle permet de réguler facilement la température des différents constituants de l'appareil, ces températures pouvant elles-mêmes être différentes;
  • - elle est basée sur un procédé sain : pas de pistolage, de projection et de formation excessive de vapeurs au point de coulée;
  • - elle permet, de contrôler la teneur en air du mélange réac- tif;
  • - elle permet d'obtenir une couche de mousse uniforme et régulière sur toute la laize (avantage important pour les plaques de faible épaisseur ou les blocs en continu à section rectangulaire);
  • - par suite de l'élimination du problème de la ligne de crème, elle permet des formulations plus simples et également d'utiliser de nouvelles matières premières;
  • elle offre la possibilité plus particulièrement pour la mousse rigide d'isolation, d'obtenir des produits composites avec parements rigides : plaques de plâtre, panneaux de bois aggloméré, contre- plaqué, feuilles de métal etc ... sans avoir à utiliser le procédé dit "inverse", qui a le gros inconvénient d'entraîner de lourdes pertes latérales de matière;
  • - elle offre la possibilité de laminer sur des supports souples : tissus, papier, films etc ...;
  • - par rapport au dispositif à goulotte fixe et à l'exception des flancs mobiles, de surface réduite, il n'y a aucune zone sans mouvement où la mousse peut se figer et nécessiter un décrochage manuel. Le risque d'icebergs est supprimé. Le problème de la propreté de la goulotte,qui est très important pour un écoulement régulier, ne se pose plus avec le dispositif mettant en oeuvre le procédé selon l'invention;
  • - l'invention permet en outre une maîtrise plus grande de la vitesse de défilement du convoyeur de coulée. Cette vitesse pouvant être notablement réduite; la longueur des installations peut être diminuée en conséquence, d'où une réduction importante des coûts d'investissements.
The advantages of the invention lie at various levels:
  • - it is simple in design and easy to adapt to all types of foaming machines;
  • - It can be used both for the manufacture of flexible foam and for the manufacture of rigid foam;
  • - it offers the possibility of varying the width continuously;
  • - also the possibility of continuously varying the volume of the liquid in retention before the start of the foaming reaction or, if necessary, the possibility of keeping this volume constant while changing the width: it is therefore not necessary to make a catalysis adjustment;
  • - It allows to easily regulate the temperature of the various components of the device, these temperatures can themselves be different;
  • - it is based on a sound process: no spraying, spraying and excessive formation of vapors at the pouring point;
  • - it makes it possible to control the air content of the reactive mixture;
  • - it makes it possible to obtain a uniform and regular layer of foam over the entire width (important advantage for the sheets of thin or continuous blocks with rectangular section);
  • - following the elimination of the problem of the cream line, it allows simpler formulations and also the use of new raw materials;
  • it offers the possibility, more particularly for rigid insulation foam, of obtaining composite products with rigid facing: plasterboard, chipboard panels, plywood, metal sheets, etc. without having to use the process. called "reverse", which has the major drawback of causing heavy lateral losses of material;
  • - it offers the possibility of laminating on flexible supports: fabrics, paper, films etc ...;
  • - compared to the device with fixed chute and with the exception of the movable sides, of reduced surface, there is no zone without movement where the foam can freeze and require a manual release. The risk of icebergs is eliminated. The problem of the cleanliness of the chute, which is very important for a regular flow, no longer arises with the device implementing the method according to the invention;
  • - The invention also allows greater control of the running speed of the casting conveyor. This speed can be significantly reduced; the length of the installations can be reduced accordingly, resulting in a significant reduction in investment costs.

Au niveau de la production des réactants générateurs de mousse et quel que soit le mode de conception du récipient selon l'invention, la paroi amont de la zone de rétention, formée soit par le cylindre arrière, soit par la paroi du bac, est toujours à une altitude supérieure à celle du cylindre avant. La paroi aval est constituée, à sa partie inférieure, par le support flexible de fond épousant la forme .du cylindre avant et à sa partie supérieure par la ligne de crème avec cette particularité que le volume retenu de liquide réactif, donc de la nappe d'écoulement qui détermine la hauteur du bloc, peut être maîtrisé dans une large mesure, environ dans µne proportion de 1 à 2.In terms of the production of foam-generating reactants and whatever the method of designing the container according to the invention, the upstream wall of the retention zone, formed either by the rear cylinder or by the wall of the tank, is always at an altitude higher than that of the front cylinder. The downstream wall is formed, at its lower part, by the flexible bottom support conforming to the shape of the front cylinder and at its upper part by the line of cream with this peculiarity that the retained volume of reactive liquid, therefore of the water table. The flow which determines the height of the block can be controlled to a large extent, approximately in a proportion of 1 to 2.

La position sensiblement horizontaledu convoyeur n'entraîne plus d'écoulement parasite de la phase liquide sous la phase en expansion, inconvénient déjà signalé sur les convoyeurs inclinés et qui oblige à une vitesse minimale. Dans le procédé proposé, la vitesse peut être réduite autant que le permet la réactivité du mélange, d'où une réduction proportionnelle de la longueur des installations.The substantially horizontal position of the conveyor no longer causes parasitic flow of the liquid phase under the expanding phase, a drawback already mentioned on inclined conveyors and which requires a minimum speed. In the proposed method, the speed can be reduced as much as the reactivity of the mixture allows, resulting in a proportional reduction in the length of the installations.

L'invention offre la possibilité de réguler la température des cylindres ou du bac. Etant rappelé que la réaction de moussage est génératrice de chaleur, il est important de pouvoir maintenir le mélange et l'appareillage à une température constante. On utilisera de préférence un fluide caloporteur traversant les cylindres et capable d'évacuer les calories produites ou, au contraire d'en apporter si nécessaire.The invention offers the possibility of regulating the temperature of the cylinders or the tank. It being recalled that the foaming reaction generates heat, it is important to be able to maintain the mixture and the equipment at a constant temperature. It is preferable to use a heat transfer fluid passing through the cylinders and capable of removing the calories produced or, on the contrary, providing them if necessary.

L'expérience ayant montré qu'une température élevée (50 à 60°) du fond flexible limitait la surdensification de la base de la mousse (2 à 3 % d'économie sur la matière) et que, par contre une température basse entre 17 et 20° retardait la distillation des agents gonflants auxiliaires (monofluotrichlorométhylène) on voit immédiatement l'intérêt de refroidir le cylindre arrière et de réchauffer le .cylindre avant.Experience having shown that a high temperature (50 to 60 °) of the flexible bottom limits the over-densification of the base of the foam (2 to 3% savings on the material) and that, on the other hand, a low temperature between 17 and 20 ° delayed the distillation of the auxiliary blowing agents (monofluotrichloromethylene) one immediately sees the advantage of cooling the rear cylinder and reheating the front cylinder.

En cours de fabrication, il est possible de faire varier la largeur du bloc de mousse par déplacement des flancs mobiles et, en même temps si besoin, de changer la position du cylindre arrière ou du bac pour conserver dans la zone de rétention le même volume de liquide ou au contraire le modifier.During manufacture, it is possible to vary the width of the foam block by moving the movable sides and, at the same time if necessary, to change the position of the rear cylinder or of the tank to keep the same volume in the retention zone. liquid or modify it.

L'arrivée du liquide réactif peut être réalisée soit par ruissellement sur une goulotte, soit en source par deux canalisations latérales traversant les flancs mobiles et constituées chacune par une série d'ajutages: concentriques de sections décroissantes de l'amont vers l'aval, de manière à ce que les ajutages aient tous une même section ou des sections voisines pour éviter toute turbulence dans le mélange liquide et assurer la répartition du.mélange dans le récipient.The arrival of the reactive liquid can be carried out either by runoff on a chute, or at the source by two lateral pipes crossing the movable sides and each constituted by a series of nozzles: concentric with decreasing sections from upstream to downstream, so that the nozzles have all the same section or neighboring sections to avoid any turbulence in the liquid mixture and to ensure the distribution of the mixture in the container.

Il est possible d'intégrer au produit une charge pulvérulente ou granulée, sèche ou imprégnée, répandue sur le cylindre arrière à l'aide par exemple, d'une trémie et d'un distributeur approprié. L'addition des charges dans la mousse de polyuréthane, qui s'est toujours heurtée aux difficultés de les acheminer dans le mélange, se trouve résolue par ce procédé. Cette caractéristique est surtout intéressante pour la fabrication de panneaux d'isolation en mousse rigide entre deux parements.It is possible to integrate a powdery or granulated, dry or impregnated charge, spread over the rear cylinder using, for example, a hopper and a suitable distributor. The addition of fillers in polyurethane foam, which has always encountered difficulties in conveying them into the mixture, is resolved by this process. This characteristic is especially interesting for the manufacture of rigid foam insulation panels between two facings.

L'appareillage tel qu'il est décrit ci-dessus peut facilement être adapté aux convoyeurs existants, notamment pour la fabrication de mousse souple, sans perdre l'avantage de la formation de la ligne de crème sur un plan horizontal.The apparatus as described above can easily be adapted to existing conveyors, in particular for the manufacture of flexible foam, without losing the advantage of the formation of the cream line on a horizontal plane.

Cette adaptation peut être étendue aux machines de production de mousse rigide, dites machines "double bande", en conservant la faculté généralement offerte par ces machines, de régler la distance entre la tête de coulée, ici la zone de rétention, et l'entrée du convoyeur double bande.This adaptation can be extended to rigid foam production machines, known as "double band" machines, while retaining the option generally offered by these machines, of adjusting the distance between the casting head, here the retention zone, and the inlet. of the double belt conveyor.

Le procédé et le dispositif selon l'invention permettent encore d'obtenir des bandes de mousse souple d'une section droite rectangulaire ne présentant aucune détérioration des flancs et ayant une face supérieure plane.

  • - L'angle de montée peut être réglé à la vue et sans retard;
  • - la face supérieure de la bande n'est pas obstruée pendant le dégazage qui marque la fin de l'expansion;
  • - la bande se forme en expansion libre sur toute sa largeur;
  • - la matière en cours d'élaboration est sous le contrôle visuel permanent des opérateurs.
The method and the device according to the invention also make it possible to obtain flexible foam strips of a rectangular cross section having no deterioration of the sides and having a flat upper face.
  • - The angle of climb can be adjusted at sight and without delay;
  • - the upper face of the strip is not obstructed during degassing which marks the end of the expansion;
  • - the strip is formed in free expansion over its entire width;
  • - the material under development is under the permanent visual control of the operators.

Le procédé et le dispositif selon l'invention permettent enfin la fabrication de plaques de mousse rigide. L'adoption d'une tête de coulée à cylindres alimentée en source, permet de placer un dispositif capable de créer des canaux longitudinaux dans l'épaisseur du panneau en formation et réaliser ainsi une importante économie de matière première.The method and the device according to the invention finally allow the manufacture of rigid foam sheets. The adoption of a source-supplied cylinder head, allows placing a device capable of creating longitudinal channels in the thickness of the panel being formed and thus achieving a significant saving of raw material.

D'autres. avantages ressortiront encore de la description suivante de divers modes préférentiels de réalisation du dispositif selon l'invention en référence au dessin annexé sur lequel :

  • - la figure 1 est une vue en élévation très schématique d'un dispositif selon l'invention pour fabriquer des bandes de mousse de polymères souples et comportant une tête de coulée à cylindres,
  • - la figure 2 est une vue en coupe du dispositif de la figure 1 suivant la ligne II II,
  • - la figure 3 est une vue en coupe schématique partielle à plus grande échelle de la partie avant du dispositif de la figure 1, illustrant la tête de coulée dans un mode d'exécution et dans sa disposition où la zone de rétention est maximale,
  • - la figure 4 est une vue schématique de la tête de coulée de la figure 3 dans sa disposition où la zone de rétention est minimale,
  • - la figure 5 est une demi-vue de dessus schématique de la tête de coulée de la figure 3,
  • - la figure 6 est une vue en élévation partielle de la partie mécanique du récipient composant la tête de coulée,
  • - la figure 7 est une vue de dessus partielle du mécanisme de la figure 6,
  • - la figure 8 est une vue en coupe schématique d'une tête de coulée dans un autre mode de réalisation et comportant un seul cylindre. Sur cette figure, le récipient est réglé pour que sa contenance soit maximale;
  • - la figure 9 est une vue en coupe schématique de la tête de coulée de la figure 8, dont le récipient est réglé pour que sa contenance soit minimale,
  • -la figure 10 est une vue en coupé longitudinale schématique d'un dispositif selon L'invention pour la fabrication de panneaux de mousse de polymère rigide,
  • - la figure 11 est une vue en coupe longitudinale schématique de la partie avant du dispositif de la figure 10, comportant des aménagements pour obtenir des panneaux rigides. comportant des canaux longitudinaux,
  • - la figure 12 est une vue de dessus d'un des noyaux formateurs desdits canaux et de ses accessoires et qui illustre la mise en oeuvre des gaines des canaux des panneaux rigides selon un mode de réalisation,
  • - la figure 13 est une vue en perspective partielle d'un panneau de mousse rigide selon l'invention,
  • - la figure 14 est une vue en coupe longitudinale d'un des conduits d'alimentation en source du mélange de réactants dans les récipients à cylindre selon l'invention,
  • - la figure 15 est une vue suivant F1 du conduit de la figure 14.
Others. advantages will also emerge from the following description of various preferred embodiments of the device according to the invention with reference to the appended drawing in which:
  • FIG. 1 is a very schematic elevation view of a device according to the invention for manufacturing strips of flexible polymer foam and comprising a casting head with cylinders,
  • FIG. 2 is a sectional view of the device in FIG. 1 along line II II,
  • FIG. 3 is a partial schematic sectional view on a larger scale of the front part of the device of FIG. 1, illustrating the casting head in an embodiment and in its arrangement where the retention zone is maximum,
  • FIG. 4 is a schematic view of the pouring head of FIG. 3 in its arrangement where the retention area is minimal,
  • - Figure 5 is a schematic half-view from above of the casting head of Figure 3,
  • FIG. 6 is a partial elevation view of the mechanical part of the container making up the casting head,
  • FIG. 7 is a partial top view of the mechanism of FIG. 6,
  • - Figure 8 is a schematic sectional view of a casting head in another embodiment and comprising a single cylinder. In this figure, the container is adjusted so that its capacity is maximum;
  • FIG. 9 is a schematic sectional view of the pouring head of FIG. 8, the container of which is adjusted so that its capacity is minimal,
  • FIG. 10 is a schematic longitudinal section view of a device according to the invention for the production of rigid polymer foam panels,
  • - Figure 11 is a schematic longitudinal sectional view of the front part of the device of Figure 10, comprising arrangements for obtaining rigid panels. having longitudinal channels,
  • FIG. 12 is a top view of one of the forming cores of said channels and of its accessories and which illustrates the use of the sheaths of the channels of the rigid panels according to one embodiment,
  • FIG. 13 is a partial perspective view of a rigid foam panel according to the invention,
  • FIG. 14 is a view in longitudinal section of one of the supply pipes at the source of the mixture of reactants in the cylinder containers according to the invention,
  • - Figure 15 is a view along F 1 of the conduit of Figure 14.

On se reporte d'abord aux figures 1 à 7 du dessin qui illustrent l'invention dans un mode de réalisation pour l'obtention de bandes de mousse de polymère souple.Reference is first made to FIGS. 1 to 7 of the drawing which illustrate the invention in an embodiment for obtaining strips of flexible polymer foam.

Le dispositif de la figure 1 se compose d'un convoyeur 1, s'étendant dans un plap sensiblement horizontal dont le brin porteur la supporte une feuille souple 2, issue d'un rouleau 3. Cette feuille 2, par exemple en papier est d'abord passée dans une tête de coulée 4 et est supportée, tout en pouvant glisser, sur un plateau intermédiaire 5, disposé entre la tête 4 et le convoyeur 1.The device of Figure 1 consists of a conveyor 1, extending in a substantially horizontal plap whose supporting strand supports a flexible sheet 2, from a roll 3. This sheet 2, for example of paper is of 'first passed through a casting head 4 and is supported, while being able to slide, on an intermediate plate 5, arranged between the head 4 and the conveyor 1.

Le plateau 5 et le brin porteur la du convoyeur 1 sont sensiblement dans le même plan. Les parois latérales du convoyeur 1 sont formées d'une manière connue par des feuilles souples 6, issues de deux rouleaux 7. Les rouleaux 7 sont disposés perpendiculairement au convoyeur 1 et les feuilles 6 sont adjacentes aux bords latéraux de la feuille horizontale 2. L'ensemble des feuilles 2/6, formant un couloir d'une section droite en U, se déplace à la vitesse du convoyeur 1 dans le sens de la flèche F. Tel que le représente le dessin, les rouleaux 7 sont par exemple situés au niveau du tambour avant lb du convoyeur 1. On reviendra plus loin sur cette figure pour compléter sa description concernant d'autres aménagements concernant l'invention.The plate 5 and the carrying strand 1a of the conveyor 1 are substantially in the same plane. The side walls of the conveyor 1 are formed in a known manner by flexible sheets 6, from two rollers 7. The rollers 7 are arranged perpendicular to the conveyor 1 and the sheets 6 are adjacent to the side edges of the horizontal sheet 2. L the set of sheets 2/6, forming a corridor of a U-shaped cross section, moves at the speed of the conveyor 1 in the direction of the arrow F. As shown in the drawing, the rollers 7 are for example located at level of the drum before lb of the conveyor 1. We will return later to this figure to complete its description concerning other arrangements relating to the invention.

Dans un mode d'exécution, la tête de coulée 4 est représentée aux figures 3 à 7 du dessin.In one embodiment, the casting head 4 is shown in Figures 3 to 7 of the drawing.

On appelle tête de coulée le dispositif dans lequel les réactants en phase liquide sont introduits en vue de leur mélange et assurant la fonction de distributeur de ce mélange liquide avant que ne se produise son expansion jusqu'à la phase finale où il prend la consistance d'une mousse.The device in which the liquid phase reactants are introduced with a view to mixing them and ensuring the function of distributor of this liquid mixture is called pouring head before its expansion occurs until the final phase where it takes the consistency of 'a foam.

Selon l'invention le procédé consiste à déterminer le volume d'un récipient pour former une zone de rétention du mélange de réactants en phase liquide et on maintient le niveau de ce mélange à un niveau légèrement supérieur au plan dans lequel se déplace la feuille 2, de telle sorte que la phase primaire de la dilatation du mélange et son expansion se produisent à l'extérieur du récipient, sur ladite feuille 2, laquelle est déplacée dans le sens de la flèche F pour amener le mélange en réaction au contact des parois du convoyeur 1/2/6 qui .donnent à la bande de mousse sa formé définitive, celle-ci étant par exemple d'une section droite rectangulaire.According to the invention the method consists in determining the volume of a container to form a retention zone for the mixture of reactants in the liquid phase and the level of this mixture is maintained at a level slightly higher than the plane in which the sheet 2 moves. , so that the primary phase of the expansion of the mixture and its expansion takes place outside the container, on said sheet 2, which is moved in the direction of arrow F to bring the mixture in reaction into contact with the walls of the conveyor 1/2/6 which give the foam strip its final shape, this being for example of a rectangular cross section.

Les figures 3 à 7 représentent un mode préférentiel de réali- sation de la tête de coulée, laquelle se compose d'un récipient 8 composé par deux cylindres de même longueur 9/10 et de deux parois latérales 11. Les cylindres 9/10 sont de diamètres différents, de telle sorte que le cylindre 9 est plus petit que le cylindre 10. Ces cylindres sont parallèles entre eux et,sont disposés horizontalement et transversalement au convoyeur 1. Le cylindre 9 est situé à proximité du plateau 5 et est très proche de l'autre cylindre 10 de manière à laisser entre eux un léger.espace pour le passage d'un film, par exemple une feuille de papier 2. Dans cette position, les cylindres sont sensiblement tangents et la ligne de tangence repérée 12 constitue la partie extrême inférieure du récipient. Celui-ci comporte deux parois avant/arrière courbes animées, lesquelles sont constituées par lesdits cylindres 9/ 10 ainsi que des parois latérales 11 qui sont disposées au-dessus des cylindres, sont parallèles entre elles et s'étendent perpendiculairement aux génératrices desdits cylindres 9/10. Leur bord inférieur est formé de deux lignes courbes lla/llb concourantes au point llc, lequel se situe au voisinage de la ligne de tangence repérée 12. La ligne lla est une ligne-circulaire d'un ràyon R1 ayant pour centre l'axe de rotation du cylindre 10. Cette ligne circulaire 11a contourne étroitement la périphérie du cylindre 10. La ligne llb est une ligne circulaire de. rayon R2, ayant pour centre l'axe de rotation du cylindre 9. La ligne circulaire 11b contourne la périphérie du cylindre 9 et est en appui sur la feuille de papier 2. La ligne courbe 11b se prolonge par une ligne droite 11d s'étendant au-dessus du plateau 5. La partie supérieure du cylindre 9 est sensiblement tangente au plan dans lequel se trouve le plateau 5 et dans lequel se déplace la feuille souple 2.Figures 3 to 7 show a preferred embodiment of the casting head, which consists of a container 8 composed of two cylinders of the same length 9/10 and two side walls 11. The cylinders 9/10 are of different diameters, so that the cylinder 9 is smaller than the cylinder 10. These cylinders are parallel to each other and are arranged horizontally and transversely to the conveyor 1. The cylinder 9 is located near the plate 5 and is very close from the other cylinder 10 so as to leave a slight space between them for the passage of a film, for example a sheet of paper 2. In this position, the cylinders are substantially tangent and the line of tangency marked 12 constitutes the lower end part of the container. This comprises two animated curved front / rear walls, which are constituted by said cylinders 9/10 as well as side walls 11 which are arranged above the cylinders, are parallel to each other and extend perpendicular to the generatrices of said cylinders 9 / 10. Their lower edge is formed by two curved lines lla / llb which converge at point llc, which is located in the vicinity of the line of tangency marked 12. Line lla is a circular line of a ryon R 1 having as its center the axis of rotation of the cylinder 10. This circular line 11a closely circumvents the periphery of the cylinder 10. The line llb is a circular line of. radius R 2 , having as its center the axis of rotation of the cylinder 9. The circular line 11b bypasses the periphery of the cylinder 9 and is supported on the sheet of paper 2. The curved line 11b is extended by a straight line 11d s' extending above the plate 5. The upper part of the cylinder 9 is substantially tangent to the plane in which the plate 5 is located and in which the flexible sheet 2 moves.

Celle-ci provient d'un rouleau 3 situé au-dessous de la tête de coulée, lequel rouleau est parallèle aux cylindres 9/10.This comes from a roller 3 located below the casting head, which roller is parallel to the cylinders 9/10.

La feuille 2 est d'abord en appui sur un premier rouleau 3a; monté à rotation libre sur la structure de la machine et est appliqué contre le cylindre 10 par un rouleau 3b. La feuille 2, issue du rouleau de papier 3 contourne d'abord partiellement le cylindre 10, passe dans l'espace 12, contourne la partie supérieure du cylindre 9 pour continuer sa course horizontalement sur le plateau 5 et le brin porteur la du convoyeur 1.The sheet 2 is first supported on a first roller 3a; mounted to rotate freely on the machine structure and is applied against the cylinder 10 by a roller 3b. The sheet 2, coming from the paper roll 3 first partially bypasses the cylinder 10, passes into the space 12, bypasses the upper part of the cylinder 9 to continue its race horizontally on the plate 5 and the carrying strand 1a of the conveyor 1 .

L'ensemble.cylindres 9/10 et parois latérales 11 est monté pivotant autour de l'axe du cylindre 9, de telle sorte que le volume de la zone de rétention du mélange 8 peut varier en fonction de la position angulaire dudit ensemble. Le débattement angulaire a est par exemple de 15°. A la position illustrée sur la figure 3, le cylindre 10, étant à sa position extrême inférieure, le volume de la zone de rétention 8 est maximum. Sur la figure 4, le cylindre 10 est à sa position extrême supérieure et le volume,de ladite zoné 8 est minimum.The set of cylinders 9/10 and side walls 11 is pivotally mounted around the axis of the cylinder 9, so that the volume of the mixture retention zone 8 can vary depending on the angular position of said set. The angular movement a is for example 15 °. At the position illustrated in Figure 3, the cylinder 10, being in its lower extreme position, the volume of the retention zone 8 is maximum. In FIG. 4, the cylinder 10 is in its extreme upper position and the volume of said zone 8 is minimum.

Comme on peut le voir sur la figure 3; l'angle formé entre la ligne 11d desdites parois latérales 11 et le plan dans lequel se déplace la feuille 2 est l'angle a de débattement du récipient par exemple 15°. Afin de réaliser l'étanchéité du récipient entre les parois latérales 11 et la feuille de papier 2, chaque paroi 11 comporte, du côté du plateau 5, une contre-plaque 13 destinée à masquer le vide existant entre la ligne 11d et la feuille 2. Cette contre-plaque 13 comporte, à sa partie inférieure, un bord circulaire 13a prolongé par une ligne droite 13b. Le bord inférieur de la plaque 13 suit ainsi le contour de la partie supérieure du cylindre 9 et se prolonge sur une partie du plateau 5. Les contre-plaques 13 comportent encore une lumière courbe 13c pour permettre leur positionnement sur les parois latérales 11 et leur fixation est âssurée par exemple au moyen de deux boulons 14 ou par tous autres moyens équivalents.As can be seen in Figure 3; the angle formed between the line 11d of said side walls 11 and the plane in which the sheet 2 moves is the angle a of movement of the container for example 15 °. In order to seal the container between the side walls 11 and the sheet of paper 2, each wall 11 comprises, on the side of the plate 5, a counter plate 13 intended to mask the vacuum existing between the line 11d and the sheet 2 This counter plate 13 has, at its lower part, a circular edge 13a extended by a straight line 13b. The lower edge of the plate 13 thus follows the contour of the upper part of the cylinder 9 and extends over part of the plate 5. The counter plates 13 also have a curved opening 13c to allow their positioning on the side walls 11 and their fixing is ensured for example by means of two bolts 14 or by any other equivalent means.

Les cylindres9/10 sont entraînés en rotation dans le sens des flèches F2 qui est également le sens du convoyeur. 1. Le cylindre 9 est entraîné à la vitesse du convoyeur 1. Le cylindre 10 tourne à une vitesse plus lente.The cylinders 9/10 are rotated in the direction of the arrows F2 which is also the direction of the conveyor. 1. The cylinder 9 is driven at the speed of the conveyor 1. The cylinder 10 rotates at a slower speed.

L'admission du mélange liquide dans le récipient 8 peut être réalisée de deux façons soit au moyen d'une tête de distribution 15 qui déverse le mélange liquide sur une goulotte de répartition 16, située au-dessus du cylindre 10, soit au moyen de deux tubulures horizontales 17 introduisant le liquide en source à travers les parois latérales du récipient. Chacune de ces tubulures traverse une des parois latérales 11 et amène le mélange de réactants sans turbulence dans le récipient.The admission of the liquid mixture into the container 8 can be carried out in two ways either by means of a dispensing head 15 which pours the liquid mixture onto a distribution chute 16, situated above the cylinder 10, or by means of two horizontal tubes 17 introducing the source liquid through the side walls of the container. Each of these tubes passes through one of the side walls 11 and brings the mixture of reactants without turbulence into the container.

Un mode de réalisation d'une telle tubulure 17 est illustré aux figures 14/15 du dessin. Elle se compose de plusieurs tubes coaxiaux 17a/17b/17c/17d mis dans le prolongement l'un de l'autre de telle sorte que l'extrémité de la tubulure 17e puisse atteindre la zone centrale de la tête de coulée quelle que soit la position des parois latérales 11 par rapport à l'axe médian de la tête. Cette tubulure est donc montée réglable dans la paroi 11 qu'elle traverse et l'étanchéité, au droit du passage dans celle-ci, est obtenue par exemple au moyen d'un joint à lèvre 17f permettant son coulissement. Chacun des tubes 17b/17c/17d réserve en combinaison avec celui dans lequel il est engagé et qu'il prolonge 17a/177b/17c, un espace annulaire 17g/17h/17k sensiblement de même section, laquelle correspondant approximativement à la section du plus petit tube 17d. Le positionnement des tubes entre eux est obtenu au moyen d'entretoises 17ℓ, réparties autour des tubes.Le mélangé à l'état liquide est ainsi réparti dans la tête de coulée selon un même débit et sans turbulence par les espaces annulaires 17g/17h/17k ainsi que par le tube central 17d.One embodiment of such tubing 17 is illustrated in Figures 14/15 of the drawing. It consists of several coaxial tubes 17a / 17b / 17c / 17d placed in the extension of each other so that the end of the tube 17e can reach the central area of the casting head whatever the position of the side walls 11 relative to the median axis of the head. This tubing is therefore mounted adjustable in the wall 11 which it passes through and the seal, at the right of passage therein, is obtained for example by means of a lip seal 17f allowing its sliding. Each of the tubes 17b / 17c / 17d reserves in combination with the one in which it is engaged and which it extends 17a / 177b / 17c, an annular space 17g / 17h / 17k substantially of the same section, which approximately corresponds to the section of the most small tube 17d. The positioning of the tubes between them is obtained by means of spacers 17ℓ, distributed around the tubes. The mixed in the liquid state is thus distributed in the casting head at the same flow rate and without turbulence by the annular spaces 17g / 17h / 17k as well as by the central tube 17d.

Uri mode de réalisation de la structure porteuse des cylindres 9/10 et des parois latérales 11 est donné en référence aux figures 6 et 7.An embodiment of the supporting structure of the cylinders 9/10 and of the side walls 11 is given with reference to FIGS. 6 and 7.

Les cylindres 9/10 sont entraînés en rotation en étant montés sur deux bras 18 parallèles entre eux et disposés de part et d'autre des cylindres. Le grand cylindre 10 est monté réglable sur les supports 18 dans des paliers 19 montés sur glissières et comportant des moyens de réglage 19a et de butée 19b pour permettre de l'éloigner ou de le rapprocher du cylindre 9, et pour l'immobiliser en position.The cylinders 9/10 are rotated by being mounted on two arms 18 parallel to each other and arranged on either side of the cylinders. The large cylinder 10 is mounted adjustable on the supports 18 in bearings 19 mounted on slides and comprising adjustment means 19a and stop 19b to allow it to move away from or closer to the cylinder 9, and to immobilize it in position .

Le cylindre 9 est monté à position fixe à une des extrémités des bras 18. L'ensemble est porté par des paliers 20 fixés au châssis de la machine. Dans cette conception les bras 18 et l'ensemble des éléments qu'ils portent peuvent pivoter autour de l'axe du cylindre 9, repéré 21. Le rouleau 3b,destiné à plaquer la feuille de papier contre le cylindre 10, est porté par deux biellettes 22, articulées par leur milieu autour d'un axe 23 porté par une patte s'étendant à la partie inférieure des bras. Les bielettes 22 sont soumises à la tension d'un ressort 24, accroché aux bras 18, de telle sorte que le rouleau 3b est pivoté du côté du cylindre 10.The cylinder 9 is mounted in a fixed position at one end of the arms 18. The assembly is carried by bearings 20 fixed to the chassis of the machine. In this design, the arms 18 and all of the elements which they carry can pivot around the axis of the cylinder 9, marked 21. The roller 3b, intended to press the sheet of paper against the cylinder 10, is carried by two rods 22, articulated by their middle around an axis 23 carried by a lug extending to the lower part of the arms. The links 22 are subjected to the tension of a spring 24, hooked to the arms 18, so that the roller 3b is pivoted on the side of the cylinder 10.

Les bras 18 sont reliés entre eux par une traverse 25 et comportent deux prolongements 26 s'étendant perpendiculairement de bas en haut. Ces deux prolongements 26 sont parallèles entre eux et portent à leur partie supérieure une tige filetée 27, dont le filetage est in- versé droite/gauche à partir de son milieu. Cette tige 27 est reliée par une de ses extrémités à des moyens pour l'entraîner en rotation.The arms 18 are interconnected by a crosspiece 25 and have two extensions 26 extending perpendicularly from bottom to top. These two extensions 26 are mutually parallel and carry at their upper part a threaded rod 27, the thread of which is reversed right / left from its middle. This rod 27 is connected by one of its ends to means for driving it in rotation.

Elle coopère avec deux manchons 29, lesquels portent chacun un bras 30 s'étendant perpendiculairement aux prolongements 26. Ces bras 30 sont parallèles aux bras 18 et portent, à leur extrémité libre, des bielles 31 à raison de deux biellettes par bras, lesquelles biellettes forment des chapes. Ces biellettes 31 sont articulées aux bras 30 et également aux parois latérales 11 qui composent le récipient. Les parois 11 ainsi guidées se placent automatiquement au-dessus et autour des cylindres 9/10, de sorte qu'elles réalisent en combinaison avec lesdits cylindres un volume de rétention d'une étanchéité acceptableIt cooperates with two sleeves 29, which each carry an arm 30 extending perpendicularly to the extensions 26. These arms 30 are parallel to the arms 18 and carry, at their free end, connecting rods 31 at the rate of two links per arm, which links form screeds. These links 31 are articulated on the arms 30 and also on the side walls 11 which make up the container. The walls 11 thus guided are automatically placed above and around the cylinders 9/10, so that they achieve, in combination with said cylinders, an retention volume of an acceptable seal.

Le débattement angulaire de l'ensemble est obtenu au moyen d'un ou plusieurs vérins à double effet 32 à fonctionnement de préférence hydraulique, articulés d'une part en 33 à l'extrémité de la structure mobile 18/25/26 et d'autre part en 34 sur une chape 35 fixée au châssis de l'appareillage.The angular movement of the assembly is obtained by means of one or more double-acting cylinders 32, preferably hydraulic, articulated on the one hand at 33 at the end of the mobile structure 18/25/26 and secondly at 34 on a yoke 35 fixed to the chassis of the apparatus.

Le choix du volume de la zone de rétention 8 est obtenu en modifiant l'angle a de la ligne XX1 sur laquelle sont les cylindres 9/10 et/ou en modifiant la longueur du récipient par déplacement des parois latérales 11, en agissant sur la vis 27. Les parois 11, guidées en translation par les supports 30, peuvent être rapprochées l'une vers l'autre ou éloignées l'une de l'autre symétriquement à l'axe longitudinal du dispositif. Le bras 30 est maintenu parallèlement au bras 18 au moyen d'une butée coulissante 36 échancrée en 36a qui lui est solidaire et qui coopère avec une glissière 37 s'étendant transversalement à la tête de coulée et qui est parallèle à la vis 27. Cette butée 36 s'étend perpen- diculàirement au bras 30 et au-dessous de celui-ci chaque bras 30 comporte une butée.The choice of the volume of the retention zone 8 is obtained by modifying the angle a of the line XX 1 on which the cylinders 9/10 are and / or by modifying the length of the container by displacement of the side walls 11, by acting on the screw 27. The walls 11, guided in translation by the supports 30, can be brought towards one another or distant from each other symmetrically to the longitudinal axis of the device. The arm 30 is held parallel to the arm 18 by means of a sliding stop 36 indented at 36a which is integral with it and which cooperates with a slide 37 extending transversely to the casting head and which is parallel to the screw 27. This stop 36 extends perpendicularly to arm 30 and below it each arm 30 has a stop.

Le réglage de l'écartement des parois latérales 11 détermine la largeur de la bande de mousse obtenue. Le mélange de réactants li- quidescontenu dans la zone de rétention 8 et dont le niveau supérieur se situe sensiblement dans le plan du plateau 5 ou légèrement au-dessus, est entraîné à l'état liquide par la feuille souple 2, de telle sorte que la dilatation et l'expansion de la mousse se produisent à l'extérieur du récipient sur le plateau 5, l'expansion totale se poursuivant sur le convoyeur 1.The adjustment of the spacing of the side walls 11 determines the width of the strip of foam obtained. The liquid reactant mixture contained in the retention zone 8 and the upper level of which is substantially in the plane of the plate 5 or slightly above, is entrained in the liquid state by the flexible sheet 2, so that the expansion and expansion of the foam occur outside the container on the tray 5, the total expansion continuing on the conveyor 1.

Dans le but de conserver le récipient dans un bon état de propreté, le cylindre 10, qui constitue la pardi arrière du récipient, est plongé partiellement dans un bac à solvant 38, disposé à la partie inférieure de la tête de coulée. Ce bac 38 comporte une raclette 39 s'étendant transversalement au cylindre et maintenue en position suivant un angle convenable pour détacher de la paroi du cylindre les particules de matière polymérisées qui auraient pu y adhérer. Comme on peut le voir sur le dessin, le bac 38 se déplace avec l'ensemble lors du réglage du volume de la zone de rétention 8 et sa forme est telle qu'aucun déversement de solvant ne peut se produire.In order to keep the container in a good state of cleanliness, the cylinder 10, which constitutes the rear pardi of the container, is partially immersed in a solvent tank 38, disposed at the lower part of the casting head. This tank 38 includes a squeegee 39 extending transversely to the cylinder and held in position at a suitable angle to detach from the wall of the cylinder the particles of polymerized material which could have adhered to it. As can be seen in the drawing, the tank 38 moves with the assembly when the volume of the retention zone 8 is adjusted and its shape is such that no spillage of solvent can occur.

Les cylindres 9/10 comportent encore des conduits 9a/10a équidistants de l'axe de rotation des cylindres et s'étendant longitudinalement, parallèment, audit axe de rotation. Les cylindres comportent à leurs extrémités des joints tournants pour assurer l'étanchéité à ces endroits. Ces conduits 9a/10a ont pour fonction de canaliser un fluide caloporteur,-par exemple de l'eau, dans le but de réchauffer ou refroidir les cylindres et corrélativement le mélange de réactants. Cette conception est intéressante du fait que, la réaction de moussage étant génératrice de chaleur, il est important de maintenir le mélange et l'appareillage à une.température constante. Elle permet notamment de contrôler la température à divers points du récipient. Par exemple, le cylindre arrière 10 peut être refroidi alors que le cylindre 9 peut être réchauffé. L'expérience a en effet montré qu'une température de 50 à 60° du fond flexible constitué par la feuille souple 2, limitait la surdensification de la base'de la mousse. Par contre, une basse température entre 17 et 20° retardait la distillation des agents gonflants auxiliaires d'où l'intérêt de refroidir le cylindre arrière 10 et de réchauffer le cylindre avant 9.The cylinders 9/10 also comprise conduits 9a / 10a equidistant from the axis of rotation of the cylinders and extending longitudinally, parallel, to said axis of rotation. The cylinders have rotating joints at their ends to seal at these locations. The purpose of these conduits 9a / 10a is to channel a heat-transfer fluid, for example water, for the purpose of heating or cool the cylinders and correspondingly the mixture of reactants. This design is advantageous because, since the foaming reaction generates heat, it is important to maintain the mixture and the equipment at a constant temperature. It allows in particular to control the temperature at various points in the container. For example, the rear cylinder 10 can be cooled while the cylinder 9 can be heated. Experience has in fact shown that a temperature of 50 to 60 ° of the flexible bottom formed by the flexible sheet 2, limits the overdensification of the base of the foam. On the other hand, a low temperature between 17 and 20 ° delayed the distillation of the auxiliary blowing agents, hence the advantage of cooling the rear cylinder 10 and heating the front cylinder 9.

Un autre mode de réalisation d'une tête de coulée selon l'invention est illustré aux figures 8 et 9 du dessin.Another embodiment of a casting head according to the invention is illustrated in Figures 8 and 9 of the drawing.

Celle-ci se compose d'un cylindre 40 entraîné en rotation dans le sens du déplacement de la bande transporteuse du convoyeur 1 et sur lequel cylindre 40 est appliquée une feuille de papier 2 provenant d'une bobine 3. L'enroulement partiel de la feuille 2 sur le cylindre 40 est obtenu au moyen d'un rouleau 41 s'étendant parallèlement audit cylindre. Comme dans le dispositif précédemment décrit, la feuille souple 2 est supportée par un plateau horizontal 5 et est prise en charge par un convoyeur également horizontal.This consists of a cylinder 40 rotated in the direction of movement of the conveyor belt of the conveyor 1 and on which cylinder 40 is applied a sheet of paper 2 from a reel 3. The partial winding of the sheet 2 on the cylinder 40 is obtained by means of a roller 41 extending parallel to said cylinder. As in the previously described device, the flexible sheet 2 is supported by a horizontal plate 5 and is supported by a conveyor also horizontal.

Le cylindre 40, recouvert de la feuille souple 2, constitue la paroi avant dû récipient dans lequel le mélange de réactants liquides est introduit. Les parois arrière et de fond du récipient et les parois latérales constituent un ensemble pouvant pivoter autour du cylindre 40 en restant étroitement appliqué par les parois latérales sur la feuille souple 2. Quelle que soit la position angulaire du récipient, sa partie supérieure est toujours à un niveau supérieur au plan du plateau 5 dans lequel se déplace la feuille 2. Outre la paroi mobile constituée par le cylindre 40, le récipient se compose d'une paroi arrière 42; laquelle suit en partie le contour du cylindre 40 et comporte à sa partie inférieure un "retour" 42a, dirigé du côté dudit cylindre. Un espace 43 est réservé entre les parties 42a et le cylindre, pour permettre le passage de la feuille souple 2. Les parois latérales 42b du récipient sont délimitées du côté du cylindre par une ligne circulaire 42bi, laquelle est prolongée à la partie supérieure du récipient par une ligne droite 42b2. Dans la position illustrée à la figure 9, cette ligne droite 42b2 est appliquée contre la feuille souple 2, ce qui assure l'étanchéité du récipient à cet endroit où le mélange, à l'état liquide, commence son expansion.The cylinder 40, covered with the flexible sheet 2, constitutes the front wall of the container into which the mixture of liquid reactants is introduced. The rear and bottom walls of the container and the side walls form an assembly which can pivot around the cylinder 40 while remaining tightly applied by the side walls to the flexible sheet 2. Whatever the angular position of the container, its upper part is always at a level higher than the plane of the plate 5 in which the sheet 2 moves. In addition to the movable wall formed by the cylinder 40, the container consists of a rear wall 42; which partially follows the contour of the cylinder 40 and has at its lower part a "return" 42a, directed towards the side of said cylinder. A space 43 is reserved between the parts 42a and the cylinder, to allow the passage of the flexible sheet 2. The side walls 42b of the container are delimited on the side of the cylinder by a circular line 42bi, which is extended to the upper part of the container by a straight line 42b 2 . In the position illustrated in the figure 9, this straight line 42b 2 is applied against the flexible sheet 2, which seals the container at this location where the mixture, in the liquid state, begins its expansion.

Afin d'assurer l'étanchéité du récipient, quelle que soit la position angulaire de sa partie constituée par les parois 42/42a/42b, le dispositif comporte,à l'intérieur du récipient et contre les faces internes des parois latérales 42b, des contre-plaques 44 qui ont pour fonction de masquer le vide existant entre les parois latérales 42b et la feuille souple 2, tel que cela est illustré notamment à la figure 8 du dessin. Les contre-plaques 44 ont une position fixe par rapport au cylindre 40 et comportent des moyens pour être réglées et fixées à une position déterminée par rapport aux parois latérales 42b du récipient. Elles comportent un bord circulaire 44a prolongé par une partie droite 44b, de telle sorte à coopérer étroitement avec la feuille souple 2. Elles adoptent la forme d'une bande recourbée à bords latéraux parallèles dont la largeur est supérieure à l'espace maximum E laissé au droit des parois latérales 42b du récipient.In order to seal the container, whatever the angular position of its part constituted by the walls 42 / 42a / 42b, the device comprises, inside the container and against the internal faces of the side walls 42b, against plates 44 which have the function of masking the vacuum existing between the side walls 42b and the flexible sheet 2, as illustrated in particular in FIG. 8 of the drawing. The counter plates 44 have a fixed position relative to the cylinder 40 and include means for being adjusted and fixed at a determined position relative to the side walls 42b of the container. They have a circular edge 44a extended by a straight part 44b, so as to cooperate closely with the flexible sheet 2. They take the form of a curved strip with parallel lateral edges whose width is greater than the maximum space E left in line with the side walls 42b of the container.

Comme la tête de coulée décrite en référence aux figures 3 à 7, le dispositif décrit aux figures 8 et 9 peut comporter une alimentation en source dans les parois latérales 42b du récipient ou au moyen d'une tête de distribution située au-dessus du récipient. Egalement les parois latérales 42b peuvent être rapprochées ou éloignées l'une de l'autre afin de déterminer la largeur de la bande de mousse à obtenir.Like the pouring head described with reference to FIGS. 3 to 7, the device described in FIGS. 8 and 9 may include a source supply in the side walls 42b of the container or by means of a dispensing head located above the container. . Also the side walls 42b can be brought closer or further apart from one another in order to determine the width of the strip of foam to be obtained.

La température du mélange de réactants liquides contenu dans le récipient peut être contrôlée par admission dans le cylindre d'un liquide caloporteur circulant dans des conduits longitudinaux comme cela à été décrit en référence à la figure 3. Comme dans le dispositif précédent comportant une tête de coulée à deux cylindres, la tête de coulée, représentée aux figures 8 et 9, permet de laisser s'écouler le mélange de réactànts à l'état liquide, à l'extérieur du récipient, 4u droit du plateau 5, l'extension de la mousse se faisant sur le plateau 5 pour se terminer sur le convoyeur 1.The temperature of the mixture of liquid reactants contained in the container can be controlled by admitting into the cylinder a heat transfer liquid circulating in longitudinal conduits as has been described with reference to FIG. 3. As in the previous device comprising a head casting with two cylinders, the casting head, shown in Figures 8 and 9, allows the reaction mixture to flow in the liquid state, outside the container, 4 u right of the tray 5, the extension foam forming on the plate 5 to end on the conveyor 1.

On se reporte de nouveau à la figure 1 du dessin sur laquelle on a illustré schématiquement l'évolution du mélange de réactants s'é- coulant en phase liquide au poste A et qui, entrant en réaction, se développe progressivement suivant une pente régulière pour adopter au point B la structure définitive d'une bande de mousse.Reference is again made to FIG. 1 of the drawing in which the evolution of the mixture of reactants flowing in the liquid phase at station A and which, entering into reaction, develops progressively along a regular slope is schematically illustrated. adopt at point B the final structure of a strip of foam.

Afin que la face supérieure 45 de la bande de mousse ainsi formée soit plane et que les angles supérieurs de la bande soient sensiblement des angles droits, il est nécessaire d'accompagner la mousse pendant son évolution entre les points A et B pour éviter que l'état d'abord visqueux puis pâteux du mélange ne provoque contre les parois du conformateur une retenue qui freine l'expansion des cellules en contact avec les parois. Le problème a été résolu selon l'invention en disposant à l'intérieur du convoyeur et contre chacune des parois latérales de celui-ci, constituées par des feuilles de papier 6, une feuille souple 46 également en papier, laquelle est déroulée dans une direction oblique tel que l'illustre la figure 1.So that the upper face 45 of the strip of foam thus formed is planar and that the upper angles of the strip are substantially right angles, it is necessary to accompany the foam during its evolution between points A and B to avoid that the he first viscous then pasty state of the mixture does not cause against the walls of the shaper a restraint which slows the expansion of the cells in contact with the walls. The problem has been solved according to the invention by placing inside the conveyor and against each of the side walls thereof, constituted by sheets of paper 6, a flexible sheet 46 also made of paper, which is unwound in one direction oblique as shown in Figure 1.

La feuille de papier 46, issue d'un rouleau 47 situé en avant et au-dessus de la tête de coulée à cylindres4 s'étend dans un plan vertical d'abord dans une direction inclinée de haut en bas jusqu'à la feuille 2 portée par le plateau 5. La feuille 46 est alors pliée autour d'un organe lb constitué par une paroi de forte épaisseur, dont le bord inférieur lc est rectiligne et s'étend parallèlement en jouxtant ladite feuille 2, de telle sorte que les parties 46a et 46b se déplacent dans des plans parallèles. La partie 46b est ainsi inclinée de bas en haut et s'enroule autour d'une bobine 48 située au-dessus du conformateur des bandes de mousse, lequel est constitué par la feuille horizontale 2 et par les deux feuilles 6 délimitant les parois latérales du convoyeur. L'inclinaison de la partie 46b est sensiblement celle de la matière 49 en cours de développement. Celle-ci est prise en charge au poste A et est accompagnée jusqu'à la fin de l'expansion au point B. La partie 46a de la feuille 46 se trouve,par rapport au couloir en U du convoyeur, derrière la partie 46b qui est au contact de la mousse. Celle-ci continue sa course à l'état de bande en étant guidée par les feuilles latérales 6 jusqu'à complète gélification.The sheet of paper 46, from a roll 47 located in front of and above the cylinder casting head 4 extends in a vertical plane first in a direction inclined up and down to the sheet 2 carried by the plate 5. The sheet 46 is then folded around a member 1b constituted by a very thick wall, the lower edge lc of which is straight and extends parallel by adjoining said sheet 2, so that the parts 46a and 46b move in parallel planes. The part 46b is thus inclined from bottom to top and is wound around a coil 48 situated above the shaping device for the strips of foam, which is constituted by the horizontal sheet 2 and by the two sheets 6 delimiting the side walls of the conveyor. The inclination of the part 46b is substantially that of the material 49 during development. This is taken care of at post A and is accompanied until the end of the expansion at point B. Part 46a of sheet 46 is located, relative to the U-shaped corridor of the conveyor, behind part 46b which is in contact with the foam. This continues its race in the strip state, being guided by the side sheets 6 until complete gelation.

On se reporte maintenant à la figure 10 du dessin qui illustre un dispositif selon l'invention pour fabriquer des panneaux de mousse rigide. Celui-ci se compose d'un convoyeur horizontal à tapis 50 s'étendant dans un plan horizontal au-dessus duquel est disposé un deuxième convoyeur 51. Les deux convoyeurs 50/51 sont parallèles entre eux et sont espacés l'qn de l'autre d'une distance d qui correspond à l'épaisseur de la plaque à obtenir.Referring now to Figure 10 of the drawing which illustrates a device according to the invention for manufacturing rigid foam panels. This consists of a horizontal conveyor belt 50 extending in a horizontal plane above which is disposed a second conveyor 51. The two conveyors 50/51 are parallel to each other and are spaced apart from the another of a distance d which corresponds to the thickness of the plate to be obtained.

Le brin inférieur 51a du convoyeur 51 est recouvert d'une feuille, par-exemple de papier 52 provenant d'une bobine 53 située en avant et au-dessus du dispositif.The lower strand 51a of the conveyor 51 is covered with a sheet, for example of paper 52 from a reel 53 located in before and above the device.

La tête de coulée à cylindre 54, qui est du type de celle décrite en référence aux figures 3 à 7, est montée sur un chariot 55 guidé par des rails 56. Le brin porteur 50a du convoyeur inférieur 50 est recouvert par une feuille de papier 57, laquelle provenant d'une bobine débitrice est mise en appui sur un rouleau 58 et est passée dans la tête de coulée 54 en entourant partiellement le cylindre avant 54a de cette dernière. La distance séparant la tête de coulée 54 du convoyeur inférieur 50 est comblée par un plateau 59 constitué de deux parties 59a/59b téléscopiques. Chacune de ces parties est constituée par une mince plaque métallique de préférence en cuivre ou en aluminium, lesquelles sont adjacentes et superposées de manière à pouvoir coulisser l'une par rapport à l'autre en fonction de la position de la tête de coulée 54 par rapport aux convoyeurs. La longueur de la plaque 59 peut ainsi être modifiée dans une proportion voisine de 1 à 2 afin de déterminer une zone d'expansion du mélange et de contrôler son expansion, le réchauffage étant assuré par une batterie d'émetteurs à.infrarouges 60 à position réglable et dont la répartition est déterminée par la longueur de zone choisie.The cylinder casting head 54, which is of the type described with reference to FIGS. 3 to 7, is mounted on a carriage 55 guided by rails 56. The carrying strand 50a of the lower conveyor 50 is covered by a sheet of paper 57, which from a supply reel is supported on a roller 58 and passed into the casting head 54 partially surrounding the front cylinder 54a of the latter. The distance separating the casting head 54 from the lower conveyor 50 is filled by a plate 59 made up of two telescopic parts 59a / 59b. Each of these parts is constituted by a thin metal plate preferably made of copper or aluminum, which are adjacent and superimposed so as to be able to slide relative to each other according to the position of the casting head 54 by report to the conveyors. The length of the plate 59 can thus be modified in a proportion close to 1 to 2 in order to determine a zone of expansion of the mixture and to control its expansion, the heating being ensured by a battery of transmitters with infrared 60 in position. adjustable and whose distribution is determined by the chosen zone length.

L'adoption d'une tête de coulée à cylindres selon l'invention, alimentée en source,qui supprime l'arrivée du mélange réactif par la partie supérieure du dispositif,a permis de concevoir un dispositif capable de créer des canaux longitudinaux dans l'épaisseur des panneaux en formation et de réaliser une importante économie de matière première.The adoption of a cylinder head according to the invention, supplied from a source, which suppresses the arrival of the reactive mixture from the upper part of the device, made it possible to design a device capable of creating longitudinal channels in the thickness of the panels being formed and a significant saving of raw material.

Un dispositif d'une telle conception est illustré aux figures 11 et 12 du dessin.A device of such a design is illustrated in Figures 11 and 12 of the drawing.

Au-dessus de la tête de coulée 54 et de la zone d'expansion 59, sont disposés parallèlement au sens de déplacement des convoyeurs 50/51, des barreaux 61, de préférence cylindriques..Ces barreaux sont d'une section inférieure à l'épaisseur des panneaux et s'étendent horizontalement au milieu de l'espace d existant entre les convoyeurs 50/51. Le dispositif comporte plusieurs barreaux 61 parallèles entre eux, lesquels sont situés dans un même plan. Les barreaux 61 sont fixés à la structure dç'la machine à des supports 62, situés à une de leurs.extrémités et s'étendant en porte à faux au-dessus de la tête de coulée 54 et entre lesdits convoyeurs 50/51 de telle sorte que leur . extrémité libre se situe sensiblement au point où la mousse prend sa consistance. Lesdits barreaux constituent les noyaux autour desquels viennent se former des gaines 63, obtenues à partir de bandes de papier 64 ou de film de polyéthylène par exemple, repliées en continu au moyen de galets formeurs coniques 65 selon un principe connu.Above the casting head 54 and the expansion zone 59, bars 61, preferably cylindrical, are arranged parallel to the direction of movement of the conveyors 50/51. These bars are of a section less than 1 'thickness of the panels and extend horizontally in the middle of the space d existing between the conveyors 50/51. The device comprises several bars 61 parallel to each other, which are located in the same plane. The bars 61 are fixed to the structure of the machine to supports 62, situated at one of their ends and extending in a cantilever above the casting head 54 and between said conveyors 50/51 of such so their. free end is located substantially at the point where the foam takes its consistency. Said bars constitute the cores around which sheaths 63 are formed, obtained from strips of paper 64 or polyethylene film for example, continuously folded by means of conical forming rollers 65 according to a known principle.

En amont de chaque barreau 61, est disposé un rouleau 66 sur lequel la feuille 64 est en appui par le dessous. Le rouleau 66 est disposé de telle sorte que la feuille vienne tangenter le barreau 61 à sa partie inférieure. Celui-ci est d'une section amoindrie et profilée à sa partie 61a pour accompagner la feuille 64 avant qu'elle soit mise au contact des galets formeurs 65. Ceux-ci sont disposés de telle sorte à mettre un des bords de la feuille en recouvrement sur l'autre, tel qu'illustré à la figure 12. La gaine ainsi constituée au niveau du poste A est fermée par collage ou par soudure au moyen de deux mollettes 67 qui appliquent les bords l'un sur l'autre. Les gaines sont entraînées à la même vitesse que les convoyeurs 50/51 initialement au moyen d'une pince d'amarrage et ensuite par la matière elle-même par adhérance de celle-ci aux gaines. La mousse en formation se développe autour des gaines 63 entre les convoyeurs 50/51 jusqu'à expansion totaleUpstream of each bar 61, is disposed a roller 66 on which the sheet 64 is supported from below. The roller 66 is arranged so that the sheet comes to tangent the bar 61 at its lower part. This is of a reduced section and profiled at its part 61a to accompany the sheet 64 before it is brought into contact with the forming rollers 65. These are arranged so as to bring one of the edges of the sheet into overlap on the other, as illustrated in FIG. 12. The sheath thus formed at the level of station A is closed by gluing or by welding by means of two knobs 67 which apply the edges to each other. The sheaths are driven at the same speed as the conveyors 50/51 initially by means of a clamping device and then by the material itself by adhesion of the latter to the sheaths. The foam in formation develops around the sheaths 63 between the conveyors 50/51 until total expansion

Le panneau obtenu à la sortie des convoyeurs comporte des canaux longitudinaux parallèles èntre eux et délimités par lesdites gaines. Un panneau ainsi obtenu est illustré à la figure 13 du dessin. La couche de mousse 68 calibrée en épaisseur entre les deux convoyeurs 50/51 est protégée sur les grandes faces du panneau par des feuilles de papier 52/57. Les canaux 69 formés par les noyaux 61 adoptent la forme de ces derniers et s'étendent dans le sens longitudinal du panneau.The panel obtained at the outlet of the conveyors comprises parallel longitudinal channels between them and delimited by said sheaths. A panel thus obtained is illustrated in Figure 13 of the drawing. The layer of foam 68 calibrated in thickness between the two conveyors 50/51 is protected on the large faces of the panel by sheets of paper 52/57. The channels 69 formed by the cores 61 adopt the shape of the latter and extend in the longitudinal direction of the panel.

A la figure 13, l'exemple représenté comporte des canaux 69 d'une section droite circulaire dont la paroi périphérique est délimitée et protégée par les gaines 63 qui adhèrent à la mousse. On précise que les gaines-63 peuvent également être constituées par des tubes rigides en carton ou en matière plastique.In FIG. 13, the example shown comprises channels 69 of a circular cross section, the peripheral wall of which is delimited and protected by the sheaths 63 which adhere to the foam. It should be noted that the sheaths-63 can also be constituted by rigid tubes made of cardboard or plastic.

Pour obtenir des panneaux comportant de telles gaines rigides, celles-ci sont acheminées successivement autour des noyaux 61. Les gaines sont fendues le long d'une génératrice et sont acheminées successivement pour être engagées à l'extrémité 61a des noyaux 61 et sont ensuite, comme décrit ci-dessus, entraînées par adhérence du produit en formation véhiculé par le convoyeur.To obtain panels comprising such rigid sheaths, these are successively routed around the cores 61. The sheaths are split along a generator and are successively routed to be engaged at the end 61a of the cores 61 and are then, as described above, driven by adhesion of the product in formation conveyed by the conveyor.

Claims (21)

1. Procédé de fabrication de bandes continues de mousse de polymères obtenues à partir d'un mélange de réactants liquides, générateur d'une mousse expansée, selon lequel on introduit en continu ledit mélange de réactants liquides dans un récipient et en ce qu'on laisse ce mélange se dilater de telle sorte qu'une fois totalement expansée, la mousse prise en charge par un convoyeur en U, animé d'un mouvement continu, adopte la forme d'une bande d'une section droite rectangulaire, caractérisé en ce qu'on détermine le volume dudit récipient pour former une zone de rétention du mélange de réactants en phase liquide et en ce que l'on maitient le niveau de ce mélange à un niveau légèrement supérieur au plan sur lequel s'écoule le mélange à l'état liquide, de telle sorte que la phase primaire de la dilatation du mélange et son expansion se produisent à l'extérieur du récipient sur une surface animée d'un mouvement continu sous l'effet du convoyeur, laquelle surface est maintenue dans un plan horizontal.1. Method for manufacturing continuous strips of polymer foam obtained from a mixture of liquid reactants, generator of expanded foam, according to which said mixture of liquid reactants is continuously introduced into a container and in that leaves this mixture to expand so that once fully expanded, the foam supported by a U-shaped conveyor, animated in a continuous movement, takes the form of a strip of a rectangular cross section, characterized in that that the volume of said container is determined to form a retention zone for the mixture of reactants in the liquid phase and that the level of this mixture is controlled to a level slightly higher than the plane over which the mixture flows liquid state, so that the primary phase of the expansion of the mixture and its expansion occur outside the container on a surface animated by a continuous movement under the effect of the conveyor, which surface is maintained in a plane h horizontal. 2. Dispositif pour réaliser des bandes de mousse de polymères obtenues à partir d'un mélange de réactants liquides générateurs d'une mousse expansée et comportant un récipient (8/42), des moyens (15/17) pour introduire en continu dans ce récipient, ledit mélange de réactants liquides et un convoyeur en U (1/2/6) animé d'un mouvement continu sur lequel la mousse est déposée pour adopter la forme d'une bande d'une section droite rectangulaire, dont le récipient comporte une paroi avant (9/40), une paroi arrière (10/42) et deux parois latérales(11/ 42b) caractérisé en ce que les parois avant (9/40) et arrière (10/42) constituent également le fond du récipient et en ce que la paroi avant, qui est située du côté du convoyeur (1/2/6) est une paroi courbe constituée par un cylindre (9/40) animé en rotation autour d'un axe horizontal dans le même sens et à la même vitesse que le convoyeur (1/2/6) et en ce que les bords (11b/42b1) des parois latérales (11/42b) situées du côté de la paroi courbe sont d'un contour circulaire et entourent partiellement le cylindre (9/40) afin de permettre le mouvement relatif du cylindre (9/40) et des autres parois (10/42142a/42b) tout en assurant l'étanchéité du récipient.2. Device for producing strips of polymer foam obtained from a mixture of liquid reactants generating an expanded foam and comprising a container (8/42), means (15/17) for continuously introducing into this container, said mixture of liquid reactants and a U-shaped conveyor (1/2/6) animated in a continuous movement on which the foam is deposited to adopt the shape of a strip of a rectangular cross section, the container of which comprises a front wall (9/40), a rear wall (10/42) and two side walls (11 / 42b) characterized in that the front (9/40) and rear (10/42) walls also constitute the bottom of the container and in that the front wall, which is located on the side of the conveyor (1/2/6) is a curved wall constituted by a cylinder (9/40) animated in rotation about a horizontal axis in the same direction and at the same speed as the conveyor (1/2/6) and in that the edges (11b / 42b 1 ) of the side walls (11 / 42b) located on the side of the courtyard wall be have a circular outline and partially surround the cylinder (9/40) in order to allow the relative movement of the cylinder (9/40) and the other walls (10 / 42142a / 42b) while ensuring the tightness of the container. 3. Dispositif selon la revendication 2, dont le bord supérieur de la paroi arrière (10/42) et des parois latérales (11/42b) du récipient se situent à un niveau suéprieur à celui de la paroi avant (9/40), caractérisé en ce que ladite paroi avant (9/40) tangente une surface horizontale (2) sur laquelle s'écoule le mélange de réactants en phase liquide, laquelle surface horizontale (2) est animée d'un mouvement continu sous l'effet du convoyeur (1/2/6).3. Device according to claim 2, the upper edge of the rear wall (10/42) and the side walls (11 / 42b) of the container are located at a level higher than that of the front wall (9/40), characterized in that said front wall (9/40) tangents a horizontal surface (2) on which the liquid reactant mixture flows, which horizontal surface (2) is animated by a continuous movement under the effect of the conveyor (1/2/6). 4. Dispositif selon l'une quelconque des revendications 2 et 3, caractérisé en ce que l'ensemble paroi arrière (10/42), parois latérales (11/42b) comporte des moyens pour obtenir son pivotement autour de l'axe dudit cylindre (9/40) dans le but d'élever ou d'abaisser ledit ensemble (10/42/11/42b) par rapport à ladite surface horizontale (2) afin de modifier le volume du récipient, et pour immobiliser en position ledit ensemble après réglage.4. Device according to any one of claims 2 and 3, characterized in that the rear wall assembly (10/42), side walls (11 / 42b) comprises means for obtaining its pivoting around the axis of said cylinder (9/40) for the purpose of raising or lowering said assembly (10/42/11 / 42b) relative to said horizontal surface (2) in order to modify the volume of the container, and to immobilize said assembly in position after adjustment. 5. Dispositif selon l'une quelconque des revendications 2 à 4, caractérisé en ce que la paroi arrière du récipient (8) est une paroi courbe constituée par un cylindre (10) entraîné en rotation dans le même sens que le cylindre avant (9), lesquels cylindres (9/10) sont montés sur deux axes parallèles.entre eux et sont sensiblement tangents, la ligne de tangence (12) constituant le fond du récipient (8) et en ce que les parois latérales (11) sont parallèles entre elles et sont au-dessus des cylindres (9/10) et leur bord inférieur est délimité par deux lignes circulaires (11a/11b) concourantes en un point (11c) situé au voisinage de ladite ligne de tangence (12), lesquelles parois latérales entourent partiellement les cylindres (9/10) afin de permettre d'une part la rotation des cylindres et d'autre part le mouvement relatif de l'ensemble cylindre arrière (10)/parois latérales (11) autour du cylindre avant (9) tout en assurant l'étanchéité du récipient (8).5. Device according to any one of claims 2 to 4, characterized in that the rear wall of the container (8) is a curved wall constituted by a cylinder (10) driven in rotation in the same direction as the front cylinder (9 ), which cylinders (9/10) are mounted on two parallel axes. between them and are substantially tangent, the line of tangency (12) constituting the bottom of the container (8) and in that the side walls (11) are parallel between them and are above the cylinders (9/10) and their lower edge is delimited by two circular lines (11a / 11b) intersecting at a point (11c) located in the vicinity of said tangency line (12), which walls side partially surround the cylinders (9/10) to allow on the one hand the rotation of the cylinders and on the other hand the relative movement of the rear cylinder (10) / side walls (11) around the front cylinder (9 ) while ensuring the tightness of the container (8). 6. Dispositif selon la revendication 5, caractérisé en ce que le cylindre arrière (10) est d'un diamètre plus grand que le cylindre avant (9) et est entraîné en rotation à une vitesse plus lente que celle dudit cylindre (9).6. Device according to claim 5, characterized in that the rear cylinder (10) is of a larger diameter than the front cylinder (9) and is rotated at a speed slower than that of said cylinder (9). 7. Dispositif selon l'une quelconque des revendications 5 et 6, caractérisé en ce que le cylindre arrière (10) est plongé dans un bac à solvant (38) et est soumis à l'action d'une raclette (39) s'étendant dans le sens longitudinal du cylindre (10) pour décoller à sa périphérie les particules polymérisées y adhérant.7. Device according to any one of claims 5 and 6, characterized in that the rear cylinder (10) is immersed in a solvent tank (38) and is subjected to the action of a squeegee (39) s' extending in the longitudinal direction of the cylinder (10) to detach the polymerized particles adhering thereto at its periphery. 8. Dispositif selon l'une quelconque des revendications 2 à 7, caractérisé en ce que chacune des parois latérales (11/42b) comporte une contre-plaque (13/44) s'étendant du côté de ladite surface horizontale (2) sur laquelle est déposé le mélange de réactants en phase liqui- de pour réaliser l'étanchéité à la jonction des parois latérales (11/42b) et de ladite surface (2), lesquelles contre-plaques (13/44) sont réglables en position sur les parois (11/42b).8. Device according to any one of claims 2 to 7, characterized in that each of the side walls (11 / 42b) comprises a counter plate (13/44) extending from the side of said horizontal surface (2) on which is deposited the liquid phase reactant mixture to seal at the junction of the side walls (11 / 42b) and said surface (2), which counter plates (13/44) are adjustable in position on the walls (11 / 42b). 9. Dispositif selon l'une quelconque des revendications 2 à 8, caractérisé en ce qu'au moins un desdits cylindres (9/10) comporte un faisceau de conduits (9a/l0a) parallèles entre eux et à l'axe de rotation du cylindre, dans lesquels conduits (9a/10a) est mis en circulation un fluide caloporteur pour élever ou abaisser la température du cylindre (9/10) et corrélativement la température du mélange de réactants en phase liquide.9. Device according to any one of claims 2 to 8, characterized in that at least one of said cylinders (9/10) comprises a bundle of conduits (9a / l0a) parallel to each other and to the axis of rotation of the cylinder, in which conduits (9a / 10a) is circulated a heat transfer fluid to raise or lower the temperature of the cylinder (9/10) and correspondingly the temperature of the mixture of reactants in liquid phase. 10. Dispositif selon l'une quelconque des revendications 2 à 9, caractérisé en ce que la paroi courbe, constituée par ledit cylindre (9/40) située à l'avant du récipient du côté du convoyeur (1, 2, 6) et la paroi arrière (10/42) du récipient, définissent un espace (12/43) dans lequel est passée une feuille souple (2), laquelle s'enroule partiellement autour dudit cylindre (9/40) sur lequel elle se déplace dans le récipient, laquelle feuille (2) poursuit sa course en étant prise en charge par le convoyeur (1,2,6) et constitue ladite surface horizontale (2) sur laquelle est déposé le mélange de réactants.10. Device according to any one of claims 2 to 9, characterized in that the curved wall, constituted by said cylinder (9/40) located at the front of the container on the side of the conveyor (1, 2, 6) and the rear wall (10/42) of the container, define a space (12/43) in which a flexible sheet (2) has passed, which partially wraps around said cylinder (9/40) on which it moves in the container, which sheet (2) continues to run while being supported by the conveyor (1,2,6) and constitutes said horizontal surface (2) on which the mixture of reactants is deposited. 11. Dispositif selon la revendication 10, caractérisé en ce que la feuille souple (2) est appliquée contre la partie inférieure dudit cylindre (40) au-dessous du fond du récipient au moyen d'un rouleau (41) soumis à l'action de moyens élastiques.11. Device according to claim 10, characterized in that the flexible sheet (2) is applied against the lower part of said cylinder (40) below the bottom of the container by means of a roller (41) subjected to the action elastic means. 12. Dispositif selon l'une quelconque des revendications 2 à 10, caractérisé en ce que la feuille souple (2) est appliquée contre la partie inférieure du cylindre arrière (10) au-dessous de la ligne de tangence (12) des deux cylindres (9/10) au moyen d'un rouleau (3b) soumis à l'action de moyens élastiques, laquelle feuille est ensuite passée entre les deux cylindres (9/10) et entoure partiellement le cylindre avant (9) par le dessus pour s'étendre tangentiellement à celui-ci dans une position sensiblement horizontale.12. Device according to any one of claims 2 to 10, characterized in that the flexible sheet (2) is applied against the lower part of the rear cylinder (10) below the line of tangency (12) of the two cylinders (9/10) by means of a roller (3b) subjected to the action of elastic means, which sheet is then passed between the two cylinders (9/10) and partially surrounds the front cylinder (9) from above to extend tangentially thereto in a substantially horizontal position. 13. Dispositif selon l'une quelconque des revendications 2 à 12, dont le mélange est introduit en source dans le récipient (8), caractérisé en ce qu'il comporte au moins une tubulure (17) traversant chacune des parois (11/42b), laquelle tubulure est montée coulissante pour être positionnée dans la tête de coulée (4) et comporte sur sa longueur des ouvertures' pour assurer la répartition du mélange à l'état liquide dans la tête de coulée.13. Device according to any one of claims 2 to 12, the mixture of which is introduced at source into the container (8), characterized in that it comprises at least one tube (17) passing through each of the walls (11 / 42b ), which tubing is slidably mounted to be positioned in the casting head (4) and has along its length openings' to ensure the distribution of the mixture in the liquid state in the casting head. 14. Dispositif selon la revendication 13, caractérisé en ce que la tubulure (17) se compose de plusieurs tubes coaxiaux (17a/17b/ 17c/17d) disposés dans le prolongement l'un de l'autre et de section dégressive par rapport à la circulation du mélange, de telle sorte à réserver entre eux des espaces annulaires (17g/17h/17k) sensiblement de même section, laquelle correspond approximativement à la section du plus petit.tube central (17d).14. Device according to claim 13, characterized in that that the tubing (17) consists of several coaxial tubes (17a / 17b / 17c / 17d) arranged in the extension of one another and of decreasing section with respect to the circulation of the mixture, so as to reserve between them annular spaces (17g / 17h / 17k) substantially of the same section, which corresponds approximately to the section of the smallest central tube (17d). 15. Dispositif selon l'une quelconque des revendications 2 à 14, dans lequel le convoyeur en U se compose d'un tapis (la) porteur de la feuille souple (2), sur laquelle se développe la mousse et dont les parois latérales (6) sont constituées par deux feuilles souples, chacune issue d'un rouleau vertical (7) situé à l'avant du dispositif du côté du récipient (4), lesquelles feuilles (6) s'étendent sur la longueur du convoyeur (I) et s'enroulent autour d'un autre rouleau vertical situé à l'arrière du dispositif, lesquelles feuilles (6) se déplaçant à la vitesse du tapis (la) en étant accolées du côté de leur bord inférieur le long des bords latéraux de ladite feuille (2), portée par le convoyeur, caractérisé en ce qu'il comporte en outre parallèlement et à proximité de chacune des faces internes des parois latérates (6) du convoyeur (1), une autre feuille souple inclinée (46) laquelle issue d'un rouleau (47) situé du côté dudit récipient (4) s'étend sur au moins la partie du dispositif où les réactants déposés en phase liquide sur ladite feuille horizontale (2) entrent en réaction et se développent jusqu'à l'expansion totale de la mousse, laquelle feuille se déplace dans cette partie (46b) suivant une direction rectiligne de l'entrée vers la sortie du dispositif et de bas en haut pour être prise en charge par le rouleau (48) situé au-dessus du convoyeur (1), son inclinaison étant telle que ses bords latéraux sont sensiblement parallèles à la pente (49) du mélange en phase de réaction afin d'obtenir des bandes de mousse ayant une face supérieure plane formant avec leurs faces latérales des arêtes vives exemptes de défaut de surface.15. Device according to any one of claims 2 to 14, in which the U-shaped conveyor consists of a mat (la) carrying the flexible sheet (2), on which the foam develops and whose side walls ( 6) consist of two flexible sheets, each from a vertical roller (7) located at the front of the device on the side of the container (4), which sheets (6) extend over the length of the conveyor (I) and wrap around another vertical roller located at the rear of the device, which sheets (6) moving at the speed of the carpet (la) being joined against the side of their lower edge along the side edges of said sheet (2), carried by the conveyor, characterized in that it further comprises, parallel to and near each of the internal faces of the lateral walls (6) of the conveyor (1), another inclined flexible sheet (46) which comes from a roller (47) located on the side of said container (4) extends over at least the part of the device o where the reactants deposited in the liquid phase on said horizontal sheet (2) enter into reaction and develop until the total expansion of the foam, which sheet moves in this part (46b) in a rectilinear direction from the inlet to the output of the device and from bottom to top to be supported by the roller (48) located above the conveyor (1), its inclination being such that its lateral edges are substantially parallel to the slope (49) of the mixture in reaction phase in order to obtain strips of foam having a flat upper face forming with their lateral faces sharp edges free from surface defects. 16. Dispositif selon la revendication 15, caractérisé en ce que les parties (46a/46b) de la feuille (46) sont situées au-dessus du convoyeur (1) et de la tête de coulée (4) et en ce que la partie (46a) est inclinée de haut en bas et est pliée le long d'un organe rectiligne parallèle et jouxtant la feuille horizontale (2) et la par- .tie (46b) est renvoyée de bas en haut suivant la même inclinaison que celle de la partie (46a).16. Device according to claim 15, characterized in that the parts (46a / 46b) of the sheet (46) are located above the conveyor (1) and the casting head (4) and in that the part (46a) is inclined from top to bottom and is folded along a parallel rectilinear member and adjoining the horizontal sheet (2) and the part (46b) is returned from bottom to top according to the same inclination as that of the part (46a). 17. Dispositif selon l'une quelconque des revendications 2 à 14 pour la fabrication de panneaux de mousse rigide et comportant un convoyeur inférieur (50) porteur d'une feuille souple (57) sur laquelle est déposé le mélange de rêactants et un deuxième convoyeur (51) disposé au-dessus dudit convoyeur inférieur (50) et parallèle à celui-ci et sur lequel est appliqué une feuille souple (52) sur le brin inférieur du tapis supérieur (51a), lesquels convoyeurs (50/51) définissent un espace d qui détermine l'épaisseur des panneaux de mousse rigide, caractérisé en ce que le récipient (54) dans lequel sont introduits les réactants liquides est déplaçable dans le sens longitudinal du dispositif et comporte des moyens pour être immobilisé en position par rapport au convoyeur (50).17. Device according to any one of claims 2 to 14 for the manufacture of rigid foam panels and comprising a lower conveyor (50) carrying a flexible sheet (57) on which is deposited the mixture of reactants and a second conveyor (51) disposed above said lower conveyor ( 50) and parallel to it and on which a flexible sheet (52) is applied to the lower strand of the upper belt (51a), which conveyors (50/51) define a space d which determines the thickness of the foam panels rigid, characterized in that the container (54) into which the liquid reactants are introduced is movable in the longitudinal direction of the device and comprises means for being immobilized in position relative to the conveyor (50). 18. Dispositif selon la revendication 17, caractérisé en ce que le plateau (59) qui s'étend entre le récipient (54) et le convoyeur inférieur (50) se compose d'au moins deux plaques (59a/59b) de faible épaisseur, parallèles entre elles et adjacentes, lesquelles plaques sont télescopiques pour ajuster la longueur du plateau (59) afin de relier le récipient (54) et le convoyeur (50).18. Device according to claim 17, characterized in that the plate (59) which extends between the container (54) and the lower conveyor (50) consists of at least two thin plates (59a / 59b) , mutually parallel and adjacent, which plates are telescopic to adjust the length of the plate (59) in order to connect the container (54) and the conveyor (50). 19. Dispositif selon l'une quelconque des revendications 2 à 14 et 17 et 18, caractérisé en ce qu'il comporte, dans l'espace existant entre le convoyeur inférieur (50) et le convoyeur supérieur (51); des barreaux (61) parallèles entre eux et disposés dans un même plan, lesquels barreaux (61) sont en porte à faux et sont fixés à la structure du dispositif du côté dudit récipient (54) et s'étendent vers les convoyeurs (50/51)'de telle sorte que leur extrémité libre qui se trouve entre lesdits convoyeurs (50/51) se situe sensiblement au lied où se produit la solidification de la mousse.19. Device according to any one of claims 2 to 14 and 17 and 18, characterized in that it comprises, in the space existing between the lower conveyor (50) and the upper conveyor (51); bars (61) parallel to each other and arranged in the same plane, which bars (61) are cantilevered and are fixed to the structure of the device on the side of said container (54) and extend towards the conveyors (50 / 51) 'so that their free end which is between said conveyors (50/51) is located substantially at the edge where the solidification of the foam occurs. 20. Dispositif selon la revendication 19, caractérisé en ce que chacun des barreaux (61) est enveloppé par une gaine (63) légèrement plus grande que le barreau, pourpouvoir être déplacée le long de celui-ci sous l'effet de la mousse pendant son expansion, afin de réaliser en continu et délimiter des canaux (69) dans les panneaux de mousse (68).20. Device according to claim 19, characterized in that each of the bars (61) is enveloped by a sheath (63) slightly larger than the bar, so that it can be moved along the latter under the effect of the foam during its expansion, in order to continuously produce and delimit channels (69) in the foam panels (68). 21. Produit nouveau consistant en un panneau de mousse rigide (68) dont les grandes faces (52/57) sont recouvertes de feuilles d'un matériau de protection, caractérisé en ce qu'il comporte dans son épaisseur des canaux (69) parallèles entre eux, dont la paroi périphérique est protégée par une gaine (63) adhérant à la mousse.21. New product consisting of a rigid foam panel (68) whose large faces (52/57) are covered with sheets of a protective material, characterized in that it has in its thickness parallel channels (69) between them, the peripheral wall of which is protected by a sheath (63) adhering to the foam.
EP82430006A 1981-03-24 1982-03-23 Method and apparatus for the manufacture of synthetic-foam sheets Expired EP0061412B1 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
AT82430006T ATE14397T1 (en) 1981-03-24 1982-03-23 PROCESS AND APPARATUS FOR THE PRODUCTION OF PLASTIC FOAM RAILS.

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
FR8106043A FR2502541A1 (en) 1981-03-24 1981-03-24 METHOD AND DEVICE FOR MANUFACTURING POLYMER FOAM BANDS AND PRODUCTS OBTAINED
FR8106043 1981-03-24

Publications (2)

Publication Number Publication Date
EP0061412A1 true EP0061412A1 (en) 1982-09-29
EP0061412B1 EP0061412B1 (en) 1985-07-24

Family

ID=9256658

Family Applications (1)

Application Number Title Priority Date Filing Date
EP82430006A Expired EP0061412B1 (en) 1981-03-24 1982-03-23 Method and apparatus for the manufacture of synthetic-foam sheets

Country Status (7)

Country Link
US (1) US4559003A (en)
EP (1) EP0061412B1 (en)
AT (1) ATE14397T1 (en)
DE (1) DE3264848D1 (en)
FR (1) FR2502541A1 (en)
NO (1) NO823917L (en)
WO (1) WO1982003357A1 (en)

Families Citing this family (17)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR2584019B1 (en) * 1985-06-28 1987-09-18 Poncet Jean DEVICE FOR MAKING POLYMER FOAM BLOCKS
IT1246263B (en) * 1990-09-07 1994-11-17 Montedipe Srl PROCEDURE FOR THE PREPARATION OF BODIES FORMED WITH INTEGRATED POLYURETHANE SKIN AND BODIES FORMED SO OBTAINED.
US5527172A (en) * 1994-04-15 1996-06-18 Carpenter Co. Apparatus for forming a foam product
US5670101A (en) * 1996-01-26 1997-09-23 Shell Oil Company Process to prepare foams from high internal phase emulsions
US5656678A (en) * 1996-05-14 1997-08-12 Hickory Springs Manufacturing Company Method and apparatus for the production of polyurethane foam using variable capacity trough
DE50006813D1 (en) * 2000-04-11 2004-07-22 Siempelkamp Handling Sys Gmbh Foam application with two-dimensionally movable application device
CA2422392A1 (en) * 2002-03-12 2003-09-12 Bombardier Inc. Cold-weather helmet with breathing mask breathing air from inside the helmet
MX2007010381A (en) 2005-02-25 2007-12-12 Nova Chem Inc Composite pre-formed building panels, a building and a framing stud.
US8752348B2 (en) 2005-02-25 2014-06-17 Syntheon Inc. Composite pre-formed construction articles
AU2006216460A1 (en) 2005-02-25 2006-08-31 Nova Chemicals Inc. Lightweight compositions and articles containing such
MX2007011640A (en) * 2005-03-22 2008-01-18 Nova Chem Inc Lightweight concrete compositions.
US7677009B2 (en) 2007-02-02 2010-03-16 Nova Chemicals Inc. Roof truss system
KR101429013B1 (en) * 2007-07-02 2014-08-11 삼성전자주식회사 METHOD FOR MANUFACTURING CONDUCTIVE TRANSFERRING ROLLER, TRANSFERRING ROLLER MANUFACTURED THEREWITH
US20090078161A1 (en) * 2007-09-20 2009-03-26 Nova Chemicals Inc. Methods of minimizing concrete cracking and shrinkage
US8048219B2 (en) * 2007-09-20 2011-11-01 Nova Chemicals Inc. Method of placing concrete
CN112025907B (en) * 2020-08-17 2025-05-30 福建省永安林业(集团)股份有限公司永安人造板厂 A lightweight flame-retardant fiberboard production system with a flame-retardant foam ball spraying device
CN119117693B (en) * 2024-11-15 2025-02-18 山东蓝海晶体科技有限公司 Full-biodegradable material transferring device and method

Citations (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR748468A (en) * 1932-01-30 1933-07-04 Advanced device for the manufacture of films and thin sheets
US3047449A (en) * 1958-01-16 1962-07-31 Du Pont Process for preparing a thin cellular polyurethane layer of uniform thickness
FR1302293A (en) * 1961-10-04 1962-08-24 Bayer Ag Method and apparatus for the production of profiles and tapes from homogeneous plastics or in the form of foam
GB965185A (en) * 1961-03-13 1964-07-29 Daniel Rosenthal Improvements relating to methods and apparatus for forming continuous tubing
FR1428114A (en) * 1965-02-12 1966-02-11 Feldmuehle Ag Process for obtaining rigid plates of synthetic foam material of low volumetric weight
US3235400A (en) * 1961-03-22 1966-02-15 Union Carbide Corp Metering foam coating
FR1560106A (en) * 1967-04-12 1969-03-14
FR2027417A1 (en) * 1968-12-31 1970-09-25 Adamson United Co
GB1260287A (en) * 1968-02-06 1972-01-12 Coolag Ltd Improvements in or relating to the manufacture of polyurethane or isocyanurate foams
FR2214572A1 (en) * 1973-01-18 1974-08-19 Mitsubishi Rayon Co
FR2330525A1 (en) * 1975-11-07 1977-06-03 Unifoam Ag MACHINE FOR THE CONTINUOUS PRODUCTION OF A STRIP IN POLYMER FOAM, THEN CUT INTO BLOCKS OF FOAM, ESPECIALLY OF POLYURETHANE FOAM

Family Cites Families (21)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE1504434B2 (en) * 1961-07-11 1970-11-05 Joh. Kleinewefers Söhne, 4150 Krefeld Method and device for the production of homogeneous, stretchable film webs from non-crystalline macromolecular plastics
US3281510A (en) * 1962-08-20 1966-10-25 Ivar C Lovret Method and apparatus for continuously molding a composite sandwich panel having regular interconnecting voids therein
US3354244A (en) * 1964-08-13 1967-11-21 Hudson Engineering Corp Method and apparatus for the manufacture of foamed plastic tubing
US3328503A (en) * 1965-03-24 1967-06-27 Union Carbide Corp Process for the manufacture of thermoplastic films
US3414641A (en) * 1965-07-30 1968-12-03 Ibm Method of fabricating resistor compositions
GB1169548A (en) * 1965-12-17 1969-11-05 Woodhall Ind Inc Process and apparatus for making Laminated Structures
US3478138A (en) * 1966-12-01 1969-11-11 Charles E Friesner Method of making thermoplastic articles having non-planar surface contours
IL30474A (en) * 1968-01-05 1972-07-26 Tenneco Chem Method and apparatus for molding foamed cellular products from a liquid reaction mixture
NL157240B (en) * 1968-04-26 1978-07-17 Selm Kunststoff Verfahren EQUIPMENT FOR THE CONTINUOUS MANUFACTURE OF TUBULAR OBJECTS EQUIPPED WITH LONG SLOTS WITH A FOAM PLASTIC CORE.
US3499957A (en) * 1968-09-11 1970-03-10 Union Carbide Corp Method for producing substantially uniform calendered material
DE1956419A1 (en) * 1968-11-23 1970-06-11 Luigi Tomasoni Method and apparatus for producing expanded plastic material or plastics material
US3681485A (en) * 1969-10-24 1972-08-01 Lieberman Abraham B Method of combining fluid components to continuously produce polyurethane form
NO131636C (en) * 1970-09-01 1975-07-02 Unifoam Ag
US3754064A (en) * 1970-09-04 1973-08-21 Armstrong Cork Co Method for making hollow tubing having an annular wall of foamed material
US3991151A (en) * 1972-06-14 1976-11-09 Schiesser Ag Method of slitting non-vulcanized rubber web upon removal from rolling mill
US3912580A (en) * 1973-10-23 1975-10-14 Envirotech Corp Method for solidifying smelt
DE2631145C2 (en) * 1976-07-10 1981-09-24 Bayer Ag, 5090 Leverkusen Method and device for applying a layer of a liquid, foamable reaction mixture to a continuously conveyed support
US4093109A (en) * 1976-09-20 1978-06-06 Schrader Milford J Expansible trough apparatus for use in producing polyurethane foam
DE2726084A1 (en) * 1977-06-10 1979-01-04 Bayer Ag PROCESS AND DEVICE FOR THE CONTINUOUS PRODUCTION OF FOAM BLOCKS WITH RECTANGULAR CROSS-SECTION
US4306927A (en) * 1978-01-26 1981-12-22 The Celotex Corporation Process for producing a laminate of metal with thermoplastic material
US4363610A (en) * 1981-01-26 1982-12-14 Miller Foam Enterprises, Inc. Apparatus for continuously molding cylindrical blocks of foamed polymeric material

Patent Citations (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR748468A (en) * 1932-01-30 1933-07-04 Advanced device for the manufacture of films and thin sheets
US3047449A (en) * 1958-01-16 1962-07-31 Du Pont Process for preparing a thin cellular polyurethane layer of uniform thickness
GB965185A (en) * 1961-03-13 1964-07-29 Daniel Rosenthal Improvements relating to methods and apparatus for forming continuous tubing
US3235400A (en) * 1961-03-22 1966-02-15 Union Carbide Corp Metering foam coating
FR1302293A (en) * 1961-10-04 1962-08-24 Bayer Ag Method and apparatus for the production of profiles and tapes from homogeneous plastics or in the form of foam
FR1428114A (en) * 1965-02-12 1966-02-11 Feldmuehle Ag Process for obtaining rigid plates of synthetic foam material of low volumetric weight
FR1560106A (en) * 1967-04-12 1969-03-14
GB1260287A (en) * 1968-02-06 1972-01-12 Coolag Ltd Improvements in or relating to the manufacture of polyurethane or isocyanurate foams
FR2027417A1 (en) * 1968-12-31 1970-09-25 Adamson United Co
FR2214572A1 (en) * 1973-01-18 1974-08-19 Mitsubishi Rayon Co
FR2330525A1 (en) * 1975-11-07 1977-06-03 Unifoam Ag MACHINE FOR THE CONTINUOUS PRODUCTION OF A STRIP IN POLYMER FOAM, THEN CUT INTO BLOCKS OF FOAM, ESPECIALLY OF POLYURETHANE FOAM

Also Published As

Publication number Publication date
WO1982003357A1 (en) 1982-10-14
FR2502541A1 (en) 1982-10-01
NO823917L (en) 1982-11-23
US4559003A (en) 1985-12-17
EP0061412B1 (en) 1985-07-24
FR2502541B1 (en) 1984-05-04
DE3264848D1 (en) 1985-08-29
ATE14397T1 (en) 1985-08-15

Similar Documents

Publication Publication Date Title
EP0061412B1 (en) Method and apparatus for the manufacture of synthetic-foam sheets
BE1008522A6 (en) Process cooling and sizing oblong objects and synthetic cooling device and calibration for the implementation process.
EP0732987B1 (en) Method and apparatus for making articles by photoprocessing a material
FR2822815A1 (en) Process, for forming insulating and watertight wall for use in marine gas transport, involves sticking together band using glue
CH395013A (en) Machine for manufacturing a composite structure
CA2004599A1 (en) Stamping process for thermoplastic composite objects and installation thereof
FR2833203A1 (en) PROCESS FOR THE MANUFACTURE BY CENTRIFUGATION OF DOUBLE-WALLED RIBS
EP0038277B1 (en) Machine for forming a tubular profile
EP1066142B1 (en) Facility for producing latex objects such as pillows
FR2470630A1 (en) Air filters prodn. system - involves applying hot adhesive to strip edges and folding in accordion pleats
FR2531905A1 (en) APPARATUS FOR MANUFACTURING CYLINDRICAL PRODUCTS IN FIBER REINFORCED THERMOSETTING RESIN AND METHOD FOR MANUFACTURING SAID PRODUCTS
FR2517591A1 (en) Continuous prod. of foam polymer blocks - esp. cylindrical or annular, using thin flexible sleeve
EP0131483A1 (en) Method and apparatus for manufacturing plastic films having good optical qualities by coating
FR2822814A1 (en) Method, for forming insulating and watertight wall, involves sticking together band using thermofusible glue.
FR2634983A1 (en) METHOD AND INSTALLATION FOR SHAPING A FOOD PRODUCT CONTINUOUS DURING HARDENING
EP4155044B1 (en) Installation for continuous production of cylindrical shells with isolating properties and associated cylindrical shells
EP0203867B1 (en) Apparatus for casting metal strips
FR2523507A1 (en) METHOD AND INSTALLATION FOR CONTINUOUS VULCANIZATION OF AN ELECTRIC CABLE
CH479340A (en) Apparatus for coating a cylinder with a resinous material, in particular a urethane resin
FR2494181A1 (en)
MC412A1 (en) Process for manufacturing panels and elements in expanded material and machine for implementing said process
EP0412984B1 (en) Adjustable seal for linear distributor
CN119238987A (en) A preparation device and method for preparing PCR composite film
BE495732A (en)
FR2519325A1 (en) Carriage for gluing lining to liquefied gas tank - travels on rails fixed by studs to wall anchors and places lining strips on insulating layer

Legal Events

Date Code Title Description
PUAI Public reference made under article 153(3) epc to a published international application that has entered the european phase

Free format text: ORIGINAL CODE: 0009012

AK Designated contracting states

Designated state(s): AT BE DE GB IT NL

17P Request for examination filed

Effective date: 19820922

ITF It: translation for a ep patent filed
GRAA (expected) grant

Free format text: ORIGINAL CODE: 0009210

AK Designated contracting states

Designated state(s): AT BE DE GB IT NL

REF Corresponds to:

Ref document number: 14397

Country of ref document: AT

Date of ref document: 19850815

Kind code of ref document: T

REF Corresponds to:

Ref document number: 3264848

Country of ref document: DE

Date of ref document: 19850829

PLBE No opposition filed within time limit

Free format text: ORIGINAL CODE: 0009261

STAA Information on the status of an ep patent application or granted ep patent

Free format text: STATUS: NO OPPOSITION FILED WITHIN TIME LIMIT

26N No opposition filed
BERE Be: lapsed

Owner name: PONCET JEAN

Effective date: 19900331

ITPR It: changes in ownership of a european patent

Owner name: CESSIONE;SUNKIST CHEMICAL MACHINERY LTD

REG Reference to a national code

Ref country code: GB

Ref legal event code: 732E

ITTA It: last paid annual fee
NLS Nl: assignments of ep-patents

Owner name: SUNKIST CHEMICAL MACHINERY LTD. TE TAIPEI, TAIWAN.

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: NL

Payment date: 20010219

Year of fee payment: 20

Ref country code: AT

Payment date: 20010219

Year of fee payment: 20

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: DE

Payment date: 20010315

Year of fee payment: 20

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: GB

Payment date: 20010316

Year of fee payment: 20

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: BE

Payment date: 20010328

Year of fee payment: 20

BE20 Be: patent expired

Free format text: 20020323 *SUNKIST CHEMICAL MACHINERY LTD (CHINESE CY OF THE CHINESE NATIONALIST REPUBLIC)

REG Reference to a national code

Ref country code: GB

Ref legal event code: IF02

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: GB

Free format text: LAPSE BECAUSE OF EXPIRATION OF PROTECTION

Effective date: 20020322

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: NL

Free format text: LAPSE BECAUSE OF EXPIRATION OF PROTECTION

Effective date: 20020323

Ref country code: AT

Free format text: LAPSE BECAUSE OF EXPIRATION OF PROTECTION

Effective date: 20020323

REG Reference to a national code

Ref country code: GB

Ref legal event code: PE20

Effective date: 20020322

NLV7 Nl: ceased due to reaching the maximum lifetime of a patent

Effective date: 20020323

NLV7 Nl: ceased due to reaching the maximum lifetime of a patent

Effective date: 20020323